Motores de combustión interna.ipynb

{
 "cells": [
  {
   "cell_type": "markdown",
   "id": "2337edc5",
   "metadata": {},
   "source": [
    "# Resolver problemas termodinámicos"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "9f47dc23",
   "metadata": {},
   "source": [
    "# PROGRAMA"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 1,
   "id": "e7a8136a",
   "metadata": {},
   "outputs": [],
   "source": [
    "import pandas as pd\n",
    "import numpy as np\n",
    "import matplotlib.pyplot as plt\n",
    "#import pint\n",
    "import sympy\n",
    "sympy.init_printing()\n",
    "%matplotlib notebook\n",
    "\n",
    "#Se importan las librerias a usar"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 2,
   "id": "7e12d355",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Se importa el archivo excel con las tablas termodinámicas\n",
    "tablasAire=pd.ExcelFile('TablasAire.xlsx')"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 3,
   "id": "b188062a",
   "metadata": {},
   "outputs": [
    {
     "data": {
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       "<table border=\"1\" class=\"dataframe\">\n",
       "  <thead>\n",
       "    <tr style=\"text-align: right;\">\n",
       "      <th></th>\n",
       "      <th>Temperatura(K)</th>\n",
       "      <th>Cp(kJ/kmol*K)</th>\n",
       "      <th>h(kJ/kmol)</th>\n",
       "      <th>s(kJ/kmol*K)</th>\n",
       "      <th>Pr</th>\n",
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       "  </thead>\n",
       "  <tbody>\n",
       "    <tr>\n",
       "      <th>0</th>\n",
       "      <td>210</td>\n",
       "      <td>29.145</td>\n",
       "      <td>-2683.3</td>\n",
       "      <td>183.799</td>\n",
       "      <td>0.3987</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1</th>\n",
       "      <td>220</td>\n",
       "      <td>29.125</td>\n",
       "      <td>-2391.9</td>\n",
       "      <td>185.155</td>\n",
       "      <td>0.4693</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2</th>\n",
       "      <td>230</td>\n",
       "      <td>29.110</td>\n",
       "      <td>-2100.7</td>\n",
       "      <td>186.449</td>\n",
       "      <td>0.5483</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>3</th>\n",
       "      <td>240</td>\n",
       "      <td>29.099</td>\n",
       "      <td>-1809.7</td>\n",
       "      <td>187.688</td>\n",
       "      <td>0.6364</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>4</th>\n",
       "      <td>250</td>\n",
       "      <td>29.091</td>\n",
       "      <td>-1518.7</td>\n",
       "      <td>188.875</td>\n",
       "      <td>0.7342</td>\n",
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       "      <th>240</th>\n",
       "      <td>2610</td>\n",
       "      <td>37.101</td>\n",
       "      <td>78853.5</td>\n",
       "      <td>264.693</td>\n",
       "      <td>6699.0000</td>\n",
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       "    <tr>\n",
       "      <th>241</th>\n",
       "      <td>2620</td>\n",
       "      <td>37.111</td>\n",
       "      <td>79222.5</td>\n",
       "      <td>264.833</td>\n",
       "      <td>6814.0000</td>\n",
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       "    <tr>\n",
       "      <th>242</th>\n",
       "      <td>2630</td>\n",
       "      <td>37.122</td>\n",
       "      <td>79593.7</td>\n",
       "      <td>264.974</td>\n",
       "      <td>6931.0000</td>\n",
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       "    <tr>\n",
       "      <th>243</th>\n",
       "      <td>2640</td>\n",
       "      <td>37.132</td>\n",
       "      <td>79965.0</td>\n",
       "      <td>265.115</td>\n",
       "      <td>7049.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>244</th>\n",
       "      <td>2650</td>\n",
       "      <td>37.342</td>\n",
       "      <td>80336.4</td>\n",
       "      <td>265.256</td>\n",
       "      <td>7169.0000</td>\n",
       "    </tr>\n",
       "  </tbody>\n",
       "</table>\n",
       "<p>245 rows × 5 columns</p>\n",
       "</div>"
      ],
      "text/plain": [
       "     Temperatura(K)  Cp(kJ/kmol*K)  h(kJ/kmol)  s(kJ/kmol*K)         Pr\n",
       "0               210         29.145     -2683.3       183.799     0.3987\n",
       "1               220         29.125     -2391.9       185.155     0.4693\n",
       "2               230         29.110     -2100.7       186.449     0.5483\n",
       "3               240         29.099     -1809.7       187.688     0.6364\n",
       "4               250         29.091     -1518.7       188.875     0.7342\n",
       "..              ...            ...         ...           ...        ...\n",
       "240            2610         37.101     78853.5       264.693  6699.0000\n",
       "241            2620         37.111     79222.5       264.833  6814.0000\n",
       "242            2630         37.122     79593.7       264.974  6931.0000\n",
       "243            2640         37.132     79965.0       265.115  7049.0000\n",
       "244            2650         37.342     80336.4       265.256  7169.0000\n",
       "\n",
       "[245 rows x 5 columns]"
      ]
     },
     "execution_count": 3,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "aireSI=pd.read_excel(tablasAire,sheet_name=0)\n",
    "aireSI\n",
    "#Index_col=0 hace que la tabla tenga de index a la columna Temperatura(K)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 4,
   "id": "4348369a",
   "metadata": {},
   "outputs": [
    {
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       "      <td>8.884</td>\n",
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       "      <td>63.490</td>\n",
       "      <td>7511.0000</td>\n",
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       "      <th>238</th>\n",
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       "      <td>63.600</td>\n",
       "      <td>7939.0000</td>\n",
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       "      <th>241</th>\n",
       "      <td>4900</td>\n",
       "      <td>8.895</td>\n",
       "      <td>35716.8</td>\n",
       "      <td>63.637</td>\n",
       "      <td>8085.0000</td>\n",
       "    </tr>\n",
       "  </tbody>\n",
       "</table>\n",
       "<p>242 rows × 5 columns</p>\n",
       "</div>"
      ],
      "text/plain": [
       "     Temperatura(R)  Cp(Btu/mol*R)  h(Btu/mol)  s(Btu/mol*R)         Pr\n",
       "0               390          6.963     -1070.8        44.147     0.4449\n",
       "1               400          6.960     -1001.2        44.323     0.4861\n",
       "2               410          6.958      -931.6        44.495     0.5300\n",
       "3               420          6.956      -862.0        44.663     0.5767\n",
       "4               430          6.955      -792.5        44.826     0.6262\n",
       "..              ...            ...         ...           ...        ...\n",
       "237            4820          8.884     35005.6        63.490  7511.0000\n",
       "238            4840          8.887     35183.4        63.527  7652.0000\n",
       "239            4860          8.889     35361.1        63.564  7794.0000\n",
       "240            4880          8.892     35538.9        63.600  7939.0000\n",
       "241            4900          8.895     35716.8        63.637  8085.0000\n",
       "\n",
       "[242 rows x 5 columns]"
      ]
     },
     "execution_count": 4,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "aireING=pd.read_excel(tablasAire,sheet_name=1)\n",
    "aireING"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 5,
   "id": "bc2e75a1",
   "metadata": {
    "scrolled": true
   },
   "outputs": [
    {
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       "      <th>4840</th>\n",
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       "      <td>35183.4</td>\n",
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       "<p>242 rows × 4 columns</p>\n",
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      ],
      "text/plain": [
       "                Cp(Btu/mol*R)  h(Btu/mol)  s(Btu/mol*R)         Pr\n",
       "Temperatura(R)                                                    \n",
       "390                     6.963     -1070.8        44.147     0.4449\n",
       "400                     6.960     -1001.2        44.323     0.4861\n",
       "410                     6.958      -931.6        44.495     0.5300\n",
       "420                     6.956      -862.0        44.663     0.5767\n",
       "430                     6.955      -792.5        44.826     0.6262\n",
       "...                       ...         ...           ...        ...\n",
       "4820                    8.884     35005.6        63.490  7511.0000\n",
       "4840                    8.887     35183.4        63.527  7652.0000\n",
       "4860                    8.889     35361.1        63.564  7794.0000\n",
       "4880                    8.892     35538.9        63.600  7939.0000\n",
       "4900                    8.895     35716.8        63.637  8085.0000\n",
       "\n",
       "[242 rows x 4 columns]"
      ]
     },
     "execution_count": 5,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "#Cambiar la columna indice ahora a temperatura\n",
    "aireINGt=aireING.set_index('Temperatura(R)')\n",
    "aireSIt=aireSI.set_index('Temperatura(K)')\n",
    "aireINGt"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 6,
   "id": "c638dbf3",
   "metadata": {},
   "outputs": [
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       "    <tr>\n",
       "      <th>8.887</th>\n",
       "      <td>4840</td>\n",
       "      <td>35183.4</td>\n",
       "      <td>63.527</td>\n",
       "      <td>7652.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>8.889</th>\n",
       "      <td>4860</td>\n",
       "      <td>35361.1</td>\n",
       "      <td>63.564</td>\n",
       "      <td>7794.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>8.892</th>\n",
       "      <td>4880</td>\n",
       "      <td>35538.9</td>\n",
       "      <td>63.600</td>\n",
       "      <td>7939.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>8.895</th>\n",
       "      <td>4900</td>\n",
       "      <td>35716.8</td>\n",
       "      <td>63.637</td>\n",
       "      <td>8085.0000</td>\n",
       "    </tr>\n",
       "  </tbody>\n",
       "</table>\n",
       "<p>242 rows × 4 columns</p>\n",
       "</div>"
      ],
      "text/plain": [
       "               Temperatura(R)  h(Btu/mol)  s(Btu/mol*R)         Pr\n",
       "Cp(Btu/mol*R)                                                     \n",
       "6.963                     390     -1070.8        44.147     0.4449\n",
       "6.960                     400     -1001.2        44.323     0.4861\n",
       "6.958                     410      -931.6        44.495     0.5300\n",
       "6.956                     420      -862.0        44.663     0.5767\n",
       "6.955                     430      -792.5        44.826     0.6262\n",
       "...                       ...         ...           ...        ...\n",
       "8.884                    4820     35005.6        63.490  7511.0000\n",
       "8.887                    4840     35183.4        63.527  7652.0000\n",
       "8.889                    4860     35361.1        63.564  7794.0000\n",
       "8.892                    4880     35538.9        63.600  7939.0000\n",
       "8.895                    4900     35716.8        63.637  8085.0000\n",
       "\n",
       "[242 rows x 4 columns]"
      ]
     },
     "execution_count": 6,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "#Cambiar la columna indice ahora a Cp\n",
    "aireINGcp=aireING.set_index('Cp(Btu/mol*R)')\n",
    "aireSIcp=aireSI.set_index('Cp(kJ/kmol*K)')\n",
    "aireINGcp"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 7,
   "id": "2e240eab",
   "metadata": {},
   "outputs": [
    {
     "data": {
      "text/html": [
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       "<table border=\"1\" class=\"dataframe\">\n",
       "  <thead>\n",
       "    <tr style=\"text-align: right;\">\n",
       "      <th></th>\n",
       "      <th>Temperatura(R)</th>\n",
       "      <th>Cp(Btu/mol*R)</th>\n",
       "      <th>s(Btu/mol*R)</th>\n",
       "      <th>Pr</th>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>h(Btu/mol)</th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "    </tr>\n",
       "  </thead>\n",
       "  <tbody>\n",
       "    <tr>\n",
       "      <th>-1070.8</th>\n",
       "      <td>390</td>\n",
       "      <td>6.963</td>\n",
       "      <td>44.147</td>\n",
       "      <td>0.4449</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>-1001.2</th>\n",
       "      <td>400</td>\n",
       "      <td>6.960</td>\n",
       "      <td>44.323</td>\n",
       "      <td>0.4861</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>-931.6</th>\n",
       "      <td>410</td>\n",
       "      <td>6.958</td>\n",
       "      <td>44.495</td>\n",
       "      <td>0.5300</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>-862.0</th>\n",
       "      <td>420</td>\n",
       "      <td>6.956</td>\n",
       "      <td>44.663</td>\n",
       "      <td>0.5767</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>-792.5</th>\n",
       "      <td>430</td>\n",
       "      <td>6.955</td>\n",
       "      <td>44.826</td>\n",
       "      <td>0.6262</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>...</th>\n",
       "      <td>...</td>\n",
       "      <td>...</td>\n",
       "      <td>...</td>\n",
       "      <td>...</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>35005.6</th>\n",
       "      <td>4820</td>\n",
       "      <td>8.884</td>\n",
       "      <td>63.490</td>\n",
       "      <td>7511.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>35183.4</th>\n",
       "      <td>4840</td>\n",
       "      <td>8.887</td>\n",
       "      <td>63.527</td>\n",
       "      <td>7652.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>35361.1</th>\n",
       "      <td>4860</td>\n",
       "      <td>8.889</td>\n",
       "      <td>63.564</td>\n",
       "      <td>7794.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>35538.9</th>\n",
       "      <td>4880</td>\n",
       "      <td>8.892</td>\n",
       "      <td>63.600</td>\n",
       "      <td>7939.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>35716.8</th>\n",
       "      <td>4900</td>\n",
       "      <td>8.895</td>\n",
       "      <td>63.637</td>\n",
       "      <td>8085.0000</td>\n",
       "    </tr>\n",
       "  </tbody>\n",
       "</table>\n",
       "<p>242 rows × 4 columns</p>\n",
       "</div>"
      ],
      "text/plain": [
       "            Temperatura(R)  Cp(Btu/mol*R)  s(Btu/mol*R)         Pr\n",
       "h(Btu/mol)                                                        \n",
       "-1070.8                390          6.963        44.147     0.4449\n",
       "-1001.2                400          6.960        44.323     0.4861\n",
       "-931.6                 410          6.958        44.495     0.5300\n",
       "-862.0                 420          6.956        44.663     0.5767\n",
       "-792.5                 430          6.955        44.826     0.6262\n",
       "...                    ...            ...           ...        ...\n",
       " 35005.6              4820          8.884        63.490  7511.0000\n",
       " 35183.4              4840          8.887        63.527  7652.0000\n",
       " 35361.1              4860          8.889        63.564  7794.0000\n",
       " 35538.9              4880          8.892        63.600  7939.0000\n",
       " 35716.8              4900          8.895        63.637  8085.0000\n",
       "\n",
       "[242 rows x 4 columns]"
      ]
     },
     "execution_count": 7,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "#Cambiar la columna indice ahora a h\n",
    "aireINGh=aireING.set_index('h(Btu/mol)')\n",
    "aireSIh=aireSI.set_index('h(kJ/kmol)')\n",
    "aireINGh"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 8,
   "id": "3ba5eefd",
   "metadata": {},
   "outputs": [
    {
     "data": {
      "text/html": [
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       "<table border=\"1\" class=\"dataframe\">\n",
       "  <thead>\n",
       "    <tr style=\"text-align: right;\">\n",
       "      <th></th>\n",
       "      <th>Temperatura(K)</th>\n",
       "      <th>Cp(kJ/kmol*K)</th>\n",
       "      <th>h(kJ/kmol)</th>\n",
       "      <th>Pr</th>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>s(kJ/kmol*K)</th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "    </tr>\n",
       "  </thead>\n",
       "  <tbody>\n",
       "    <tr>\n",
       "      <th>183.799</th>\n",
       "      <td>210</td>\n",
       "      <td>29.145</td>\n",
       "      <td>-2683.3</td>\n",
       "      <td>0.3987</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>185.155</th>\n",
       "      <td>220</td>\n",
       "      <td>29.125</td>\n",
       "      <td>-2391.9</td>\n",
       "      <td>0.4693</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>186.449</th>\n",
       "      <td>230</td>\n",
       "      <td>29.110</td>\n",
       "      <td>-2100.7</td>\n",
       "      <td>0.5483</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>187.688</th>\n",
       "      <td>240</td>\n",
       "      <td>29.099</td>\n",
       "      <td>-1809.7</td>\n",
       "      <td>0.6364</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>188.875</th>\n",
       "      <td>250</td>\n",
       "      <td>29.091</td>\n",
       "      <td>-1518.7</td>\n",
       "      <td>0.7342</td>\n",
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       "    <tr>\n",
       "      <th>...</th>\n",
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       "      <td>...</td>\n",
       "      <td>...</td>\n",
       "      <td>...</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>264.693</th>\n",
       "      <td>2610</td>\n",
       "      <td>37.101</td>\n",
       "      <td>78853.5</td>\n",
       "      <td>6699.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>264.833</th>\n",
       "      <td>2620</td>\n",
       "      <td>37.111</td>\n",
       "      <td>79222.5</td>\n",
       "      <td>6814.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>264.974</th>\n",
       "      <td>2630</td>\n",
       "      <td>37.122</td>\n",
       "      <td>79593.7</td>\n",
       "      <td>6931.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>265.115</th>\n",
       "      <td>2640</td>\n",
       "      <td>37.132</td>\n",
       "      <td>79965.0</td>\n",
       "      <td>7049.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>265.256</th>\n",
       "      <td>2650</td>\n",
       "      <td>37.342</td>\n",
       "      <td>80336.4</td>\n",
       "      <td>7169.0000</td>\n",
       "    </tr>\n",
       "  </tbody>\n",
       "</table>\n",
       "<p>245 rows × 4 columns</p>\n",
       "</div>"
      ],
      "text/plain": [
       "              Temperatura(K)  Cp(kJ/kmol*K)  h(kJ/kmol)         Pr\n",
       "s(kJ/kmol*K)                                                      \n",
       "183.799                  210         29.145     -2683.3     0.3987\n",
       "185.155                  220         29.125     -2391.9     0.4693\n",
       "186.449                  230         29.110     -2100.7     0.5483\n",
       "187.688                  240         29.099     -1809.7     0.6364\n",
       "188.875                  250         29.091     -1518.7     0.7342\n",
       "...                      ...            ...         ...        ...\n",
       "264.693                 2610         37.101     78853.5  6699.0000\n",
       "264.833                 2620         37.111     79222.5  6814.0000\n",
       "264.974                 2630         37.122     79593.7  6931.0000\n",
       "265.115                 2640         37.132     79965.0  7049.0000\n",
       "265.256                 2650         37.342     80336.4  7169.0000\n",
       "\n",
       "[245 rows x 4 columns]"
      ]
     },
     "execution_count": 8,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "#Cambiar la columna indice ahora a s\n",
    "aireINGs=aireING.set_index('s(Btu/mol*R)')\n",
    "aireSIs=aireSI.set_index('s(kJ/kmol*K)')\n",
    "aireSIs"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 9,
   "id": "2c01fdc3",
   "metadata": {},
   "outputs": [
    {
     "data": {
      "text/html": [
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       "<table border=\"1\" class=\"dataframe\">\n",
       "  <thead>\n",
       "    <tr style=\"text-align: right;\">\n",
       "      <th></th>\n",
       "      <th>Temperatura(R)</th>\n",
       "      <th>Cp(Btu/mol*R)</th>\n",
       "      <th>h(Btu/mol)</th>\n",
       "      <th>s(Btu/mol*R)</th>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>Pr</th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "    </tr>\n",
       "  </thead>\n",
       "  <tbody>\n",
       "    <tr>\n",
       "      <th>0.4449</th>\n",
       "      <td>390</td>\n",
       "      <td>6.963</td>\n",
       "      <td>-1070.8</td>\n",
       "      <td>44.147</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>0.4861</th>\n",
       "      <td>400</td>\n",
       "      <td>6.960</td>\n",
       "      <td>-1001.2</td>\n",
       "      <td>44.323</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>0.5300</th>\n",
       "      <td>410</td>\n",
       "      <td>6.958</td>\n",
       "      <td>-931.6</td>\n",
       "      <td>44.495</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>0.5767</th>\n",
       "      <td>420</td>\n",
       "      <td>6.956</td>\n",
       "      <td>-862.0</td>\n",
       "      <td>44.663</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>0.6262</th>\n",
       "      <td>430</td>\n",
       "      <td>6.955</td>\n",
       "      <td>-792.5</td>\n",
       "      <td>44.826</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>...</th>\n",
       "      <td>...</td>\n",
       "      <td>...</td>\n",
       "      <td>...</td>\n",
       "      <td>...</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>7511.0000</th>\n",
       "      <td>4820</td>\n",
       "      <td>8.884</td>\n",
       "      <td>35005.6</td>\n",
       "      <td>63.490</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>7652.0000</th>\n",
       "      <td>4840</td>\n",
       "      <td>8.887</td>\n",
       "      <td>35183.4</td>\n",
       "      <td>63.527</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>7794.0000</th>\n",
       "      <td>4860</td>\n",
       "      <td>8.889</td>\n",
       "      <td>35361.1</td>\n",
       "      <td>63.564</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>7939.0000</th>\n",
       "      <td>4880</td>\n",
       "      <td>8.892</td>\n",
       "      <td>35538.9</td>\n",
       "      <td>63.600</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>8085.0000</th>\n",
       "      <td>4900</td>\n",
       "      <td>8.895</td>\n",
       "      <td>35716.8</td>\n",
       "      <td>63.637</td>\n",
       "    </tr>\n",
       "  </tbody>\n",
       "</table>\n",
       "<p>242 rows × 4 columns</p>\n",
       "</div>"
      ],
      "text/plain": [
       "           Temperatura(R)  Cp(Btu/mol*R)  h(Btu/mol)  s(Btu/mol*R)\n",
       "Pr                                                                \n",
       "0.4449                390          6.963     -1070.8        44.147\n",
       "0.4861                400          6.960     -1001.2        44.323\n",
       "0.5300                410          6.958      -931.6        44.495\n",
       "0.5767                420          6.956      -862.0        44.663\n",
       "0.6262                430          6.955      -792.5        44.826\n",
       "...                   ...            ...         ...           ...\n",
       "7511.0000            4820          8.884     35005.6        63.490\n",
       "7652.0000            4840          8.887     35183.4        63.527\n",
       "7794.0000            4860          8.889     35361.1        63.564\n",
       "7939.0000            4880          8.892     35538.9        63.600\n",
       "8085.0000            4900          8.895     35716.8        63.637\n",
       "\n",
       "[242 rows x 4 columns]"
      ]
     },
     "execution_count": 9,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "#Cambiar la columna indice ahora a Pr\n",
    "aireINGpr=aireING.set_index('Pr')\n",
    "aireSIpr=aireSI.set_index('Pr')\n",
    "aireINGpr"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 10,
   "id": "02142640",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Diccionarios y listas globales para cambiar string de mol a lb o kg\n",
    "dictLb={\"Cp(Btu/mol*R)\":\"Cp(Btu/lb*R)\",\"h(Btu/mol)\":\"h(Btu/lb)\",\"s(Btu/mol*R)\":\"s(Btu/lb*R)\"} #La masa son libras para sistemaIn\n",
    "dictGr={'Cp(kJ/kmol*K)':\"Cp(kJ/kg*K)\", 'h(kJ/kmol)':\"h(kJ/kg)\", 's(kJ/kmol*K)':\"s(kJ/kg*K)\"} #La masa son gramos\n",
    "listConvLb=[\"Cp(Btu/mol*R)\",\"h(Btu/mol)\",\"s(Btu/mol*R)\"] #Columnas que conllevan el valor mol y cambiaran el valor al convertir\n",
    "listConvGr=['Cp(kJ/kmol*K)', 'h(kJ/kmol)', 's(kJ/kmol*K)']"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "0a228a7c",
   "metadata": {},
   "source": [
    "## CONVERSIÓN DE UNIDADES ---------------------------------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 11,
   "id": "92435e93",
   "metadata": {},
   "outputs": [],
   "source": [
    "#u=pint.UnitRegistry() #Registrará las unidades \n",
    "#Q=u.Quantity #Cantidades\n",
    "#aireSecoMolSI=28.9647*u('g/mol') #1 mol de aire seco equivale a 28.9647gramos\n",
    "#aireSecoMolING=28.9647*u('lb/mol') #1 mol de aire seco equivale a 28.9647libras\n",
    "#u.default_format = \"~P\" #Para que se vean las unidades \"pretty\"\n",
    "aireSecoMol=28.9647"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "ab85141b",
   "metadata": {},
   "source": [
    "## FIN DE CONVERSIÓN DE UNIDADES -----------------------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "f0220812",
   "metadata": {},
   "source": [
    "## FUNCIONES RAÍZ -------------------------------------------------------------------------------------------------------\n",
    "Funciones raíz son las funciones que son independientes, pero muy importantes para las demás funciones complemento"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 12,
   "id": "438068a1",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Definir función que me permita obtener indices anterior y posterior al valor ingresado\n",
    "def IndexCercanos (val,df):\n",
    "    \"\"\"Definir función que me permita obtener indices anterior y posterior al valor ingresado\n",
    "    val = valor anterior y posterior a buscar en el indice\n",
    "    df = Nombre de la tabla a buscar\"\"\"\n",
    "    \n",
    "    if val not in df.index: #Buscara si el valor no está en el dataframe\n",
    "        indexCercan1=df.index.get_indexer([val],method='ffill') #Valor anterior\n",
    "        indexCercan2=df.index.get_indexer([val],method='bfill') #Valor posterior\n",
    "        indexCercano=np.append(indexCercan1,[indexCercan2,indexCercan2+1]) #+1 porque cuando el nuevo valor de temperatura se agregue, obtendra el valor de indexCercanos2\n",
    "    else: #Si el valor se encuentra en el index\n",
    "        indexCercan1=df.index.get_indexer([val]) #Array con posición exacta del index\n",
    "        indexCercano=np.append(indexCercan1,[indexCercan1-1,indexCercan1+1]) #Array con un valor menos y un valor más\n",
    "        indexCercano=np.sort(indexCercano) #Organizar array\n",
    "    return indexCercano\n",
    "    "
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 13,
   "id": "9774695c",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Definir función que me permita llamar alguna tabla termodinamica con el indice deseado\n",
    "def TablaTermodinamica(nombreTabla,n,cp=0):\n",
    "    \"\"\"Función que me permite usar en cualquier función que se dedique a encontrar valores termodinámicos\n",
    "    nombreTabla=Nombre de la tabla a llamar\n",
    "    n=propiedad extensiva PE. temperatura, entalpia, entropia, Pr PERO NO CP ya que no es monotonica\n",
    "    cp=0 P.E cp=1 hace que se adapte para las cp\n",
    "    mass='mol' por defecto\n",
    "    mass='lb'\n",
    "    mass='kg'\"\"\"\n",
    "    \n",
    "\n",
    "    #tablasMol=np.array(['Temperatura(R)', 'Cp(Btu/mol*R)', 'h(Btu/mol)', 's(Btu/mol*R)', 'Pr'])\n",
    "    #nombreTabla=nombreTabla.set_axis(tablasMol,axis=\"Columns\",copy=False)\n",
    "    n=float(n)\n",
    "    if cp==0:\n",
    "        indexes=IndexCercanos(n,nombreTabla) #Valor para localizar el indice anterior y posterior al valor de n\n",
    "        if n not in nombreTabla.index: #Busca que el valor de n no exista, si existe entonces se salta lo que lleva sangria\n",
    "            nombreTabla.loc[n]=[np.NaN,np.NaN,np.NaN,np.NaN] #Se crea una fila con la n sin valores\n",
    "            nombreTabla=nombreTabla.sort_index() #Se ordena basandose en su posición n\n",
    "            nombreTabla=nombreTabla.interpolate(method='slinear') #Se interpola los valores NaN\n",
    "            nombreTabla=nombreTabla.interpolate(method=\"slinear\",fill_value=\"extrapolate\",limit_direction=\"both\")\n",
    "            #print(nombreTabla.iloc[indexes])\n",
    "        return nombreTabla,nombreTabla.iloc[indexes]\n",
    "    else:\n",
    "        if n not in nombreTabla.index:\n",
    "            nombreTabla.loc[n]=[np.NaN,np.NaN,np.NaN,np.NaN]\n",
    "            nombreTabla=nombreTabla.sort_index()\n",
    "            nombreTabla=nombreTabla.interpolate(method='slinear')\n",
    "        return nombreTabla,nombreTabla.loc[n]\n",
    "\n",
    "    \"\"\"elif mass ==\"lb\":\n",
    "        tablasLb=np.array(['Temperatura(R)','Cp(Btu/lb*R)','h(Btu/lb)','s(Btu/lb*R)','Pr'])\n",
    "        nombreTabla\n",
    "        nombreTabla=nombreTabla.set_axis(tablasLb,axis=\"Columns\", copy=True)\n",
    "        \n",
    "        if cp==0:\n",
    "            \n",
    "        else:\n",
    "            \n",
    "        \n",
    "    elif mass ==\"kg\":\n",
    "        tablasKg=np.array(['Temperatura(K)', 'Cp(kJ/kg*K)', 'h(kJ/kg)', 's(kJ/kg*K)', 'Pr'])\n",
    "        nombreTabla=nombreTabla.set_axis(tablasKg,axis=\"Columns\", copy=True)\n",
    "        \n",
    "        if cp==0:\n",
    "            \n",
    "        else:\n",
    "    \"\"\" \n",
    "    \n",
    "    "
   ]
  },
  {
   "cell_type": "markdown",
   "id": "0dc28977",
   "metadata": {},
   "source": [
    "## FIN DE FUNCIONES RAÍZ ---------------------------------------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "314ad013",
   "metadata": {},
   "source": [
    "## FUNCIONES COMPLEMENTO ---------------------------------------------------------------------------------------\n",
    "Las funciones complemento son funciones dependientes a las raíz, necesitan de las funciones raíz para funcionar"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "68dd6ffd",
   "metadata": {},
   "source": [
    "### FUNCIONES BASADOS EN SISITEMA INGLÉS --------------------------------------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 14,
   "id": "e2a21ff1",
   "metadata": {},
   "outputs": [],
   "source": [
    "def TemperaturaING(TR):\n",
    "    \"\"\"Valores termodinámicos en función de su temperatura Rankine\n",
    "    TR = RANKINE\"\"\"\n",
    "    global aireINGt\n",
    "#   Se declara la variable global aireINGt para ser modificada globalmente\n",
    "    aireINGt,tablaIndex = TablaTermodinamica(aireINGt,TR)\n",
    "#   Debido que la función TablaTermodinamica retorna 2 valores, se les asigna el valor del primero, que\n",
    "#es la modificación global de la tabla del aire con valores de temperatura para que la interpolación se agregue.\n",
    "#La otra es una tabla visual para que al pedir un valor a la tablatermodinamica se pueda visualizar la interpolación\n",
    "    return tablaIndex\n",
    "#La tabla será lo único que se podrá visualizar al llamar a la función, esto se repite para las demás funciones\n",
    "\n",
    "def TemperaturaINGLb(TR):\n",
    "    \"\"\"Valores termodinámicos en función de su temperatura Rankine y con valores de libras en lugar de mol\n",
    "    TR = RANKINE\"\"\"\n",
    "    global dictLb,listConvLb,aireSecoMolING\n",
    "#   Aquí no es necesario asignar globalmente todas las librerias, pero aún así lo hice\n",
    "    tablaIndex = TemperaturaING(TR).copy()\n",
    "    #Genero una copia de la tabla entregada en la función de TemperarutaING\n",
    "        #tablaIndex.loc[:,listConvLb] = tablaIndex.loc[:,listConvLb]/aireSecoMol Forma anticuada\n",
    "    tablaIndex.loc[:,listConvLb]/=aireSecoMol\n",
    "    #Asigno a la variable tablaIndex que sus valores se dividan sobre la conversión de aire seco\n",
    "    tablaIndex = tablaIndex.rename(dictLb,axis=1)\n",
    "    #Le agrego el nombre a las columnas que había ya asignado en un diccionario anteriormente\n",
    "    return tablaIndex\n",
    "    \n",
    "    \n",
    "    \n"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 15,
   "id": "7f9c04d9",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Valores termodinámicos en función de Cp Inglesas\n",
    "def CpING(CP):\n",
    "    \"\"\"Valores termodinámicos en función de Cp Inglesas\n",
    "    CP = Capacidad calorifica en Btu/mol*R\"\"\"\n",
    "    global aireINGcp\n",
    "#   Se declara la variable global aireINGt para ser modificada globalmente\n",
    "    aireINGcp,tablaIndex = TablaTermodinamica(aireINGcp,CP,cp=1) #Series\n",
    "    return tablaIndex\n",
    "\n",
    "def CpINGLb(CP):\n",
    "    \"\"\"Valores termodinamicos en función de Cp inglesas con masa = Lb\n",
    "    CP = Capacidad calorifica en Btu/lb*R\"\"\"\n",
    "    global dictLb,listConvLb,aireSecoMolING\n",
    "    CP=CP*aireSecoMol\n",
    "    #Se convierten el CP ingresado a valores de CP en función de mol\n",
    "    tablaIndex = CpING(CP).copy()\n",
    "    #Explicado en def TemperaturaINGLb(TR)\n",
    "    tablaIndex = tablaIndex.set_axis(['Temperatura(R)','h(Btu/lb)','s(Btu/lb*R)','Pr'])\n",
    "    #Se cambia el nombre del eje debido a que esta función es Serie en lugar de DataFrame\n",
    "    tablaIndex.loc[['h(Btu/lb)','s(Btu/lb*R)']] /= aireSecoMol\n",
    "    #Explicado en def TemperaturaINGLb(TR)\n",
    "    return tablaIndex\n",
    "    \"\"\"Valores termodinámicos en función de Cp inglesas y con valores de libras en lugar de mol\n",
    "    CP= Capacidad calorifica en Btu/lb*R\"\"\"\n",
    "    #TablaTermodinamica(aireINGcp,CP,cp=1,mass=\"lb\")\n",
    "    "
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 16,
   "id": "c4363108",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Valores termodinámicos en función de entalpia (h) Inglesas\n",
    "def EntalpiaING(H):\n",
    "    \"\"\"Valores termodinámicos en función de entalpía(h) inglesas\n",
    "    H = entalpía (Btu/mol)\"\"\"\n",
    "    global aireINGh\n",
    "    aireINGh,tablaIndex = TablaTermodinamica(aireINGh,H) \n",
    "    return tablaIndex\n",
    "#Explicado en def TemperaturaING(TR) \n",
    "\n",
    "def EntalpiaINGLb(H):\n",
    "    \"\"\"Valores termodinámicos en función de entalpia(h) inglesas y con valores de libras en lugar de mol\n",
    "    H = Entalpía (Btu/lb)\"\"\"\n",
    "    global dictLb\n",
    "    #Aquí ya me di cuenta que no era necesario ninguna variable global ya que no serán modificadas, solo llamadas\n",
    "    H=H*aireSecoMol\n",
    "    #Explicado en def TemperaturaINGLb(TR)\n",
    "    tablaIndex = EntalpiaING(H).copy()\n",
    "    #Explicado en def TemperaturaINGLb(TR)\n",
    "    tablaIndex.reset_index(inplace=True)\n",
    "    #La columna que esta sirviendo como indice (entalpia) se regresa en forma de columna para que se pueda dividir y cambiar\n",
    "    #nombre\n",
    "    tablaIndex.loc[:,listConvLb]/=aireSecoMol\n",
    "    #Explicado en def TemperaturaINGLb(TR)\n",
    "    tablaIndex = tablaIndex.rename(dictLb,axis=1)\n",
    "    #Explicado en def TemperaturaINGLb(TR)\n",
    "    tablaIndex.set_index('h(Btu/lb)',inplace=True)\n",
    "    #Regresa la columna (entalpia) a ser el indice de la tabla\n",
    "    return tablaIndex\n",
    "    "
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 17,
   "id": "ac08eeda",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Valores termodinámicos en función de entropia (s) Inglesas\n",
    "def EntropiaING(S):\n",
    "    \"\"\"Valores termodinámicos en función de entropia(s) inglesas\n",
    "    S = entropía (Btu/mol*R)\"\"\"\n",
    "    global aireINGs\n",
    "    aireINGs,tablaIndex = TablaTermodinamica(aireINGs,S)\n",
    "    return tablaIndex\n",
    "#Explicado en def TemperaturaING(TR)\n",
    "\n",
    "def EntropiaINGLb(S):\n",
    "    \"\"\"Valores termodinámicos en función de entropia(s) inglesas y con valores de libras en lugar de mol\n",
    "    S = entropía (Btu/lb*R)\"\"\"\n",
    "    \n",
    "    global dictLb\n",
    "    S=S*aireSecoMol\n",
    "    tablaIndex = EntropiaING(S).copy()\n",
    "    tablaIndex.reset_index(inplace=True)\n",
    "    tablaIndex.loc[:,listConvLb]/=aireSecoMol\n",
    "    tablaIndex = tablaIndex.rename(dictLb,axis=1)\n",
    "    tablaIndex.set_index('s(Btu/lb*R)',inplace=True)\n",
    "    return tablaIndex\n",
    "#Explicado en def TemperaturaINGLb(TR) y EntalpiaINGLb(H)\n",
    "    "
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 18,
   "id": "a36347cd",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Valores termodinámicos en función de su presion relativa (Pr) Inglesas\n",
    "def PresionRelING(PR):\n",
    "    \"\"\"Valores termodinámicos en función de su presión relativa(Pr) inglesas\n",
    "    PR = presión relativa\"\"\"\n",
    "    global aireINGpr\n",
    "    aireINGpr,tablaIndex = TablaTermodinamica(aireINGpr,PR)\n",
    "    return tablaIndex\n",
    "#Explicado en def TemperaturaING(TR)\n",
    "\n",
    "def PresionRelINGLb(PR):\n",
    "    \"\"\"Valores termodinamicos en función de su presión relativa(Pr) inglesas y con valores de libras en lugar de mol\n",
    "    PR = Presión relativa\"\"\"\n",
    "    global dictLb\n",
    "    tablaIndex = PresionRelING(PR).copy()\n",
    "    tablaIndex.loc[:,listConvLb]/=aireSecoMol\n",
    "    tablaIndex = tablaIndex.rename(dictLb,axis=1)\n",
    "    return tablaIndex\n",
    "#Explicado en def TemperaturaINGLb(TR) y EntalpiaINGLb(H)\n",
    "    "
   ]
  },
  {
   "cell_type": "markdown",
   "id": "84d1cd05",
   "metadata": {},
   "source": [
    "### FIN DE FUNCIONES BASADO EN EL SISTEMA INGLÉS -------------------------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "33043d95",
   "metadata": {},
   "source": [
    "### FUNCIONES BASADO EN EL SISTEMA INTERNACIONAL (SI) -----------------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 19,
   "id": "4967f0d5",
   "metadata": {},
   "outputs": [],
   "source": [
    "#valores termodinámicos en función de su temperatura SI\n",
    "def TemperaturaSI(TK):\n",
    "    \"\"\"Valores termodinámicos en función de su temperatura kelvin\n",
    "    TK = Temperatura kelvin\"\"\"\n",
    "    global aireSIt\n",
    "    aireSIt,tablaIndex =  TablaTermodinamica(aireSIt,TK)\n",
    "    return tablaIndex\n",
    "#Explicado en def TemperaturaING(TR)\n",
    "\n",
    "def TemperaturaSIKg(TK):\n",
    "    \"\"\"Valores termodinamicos en función de su temperatura Kelvin\n",
    "    Y entrega valores de masa=kg\n",
    "    TK = Temperatura Kelvin\"\"\"\n",
    "    global dictGr,listConvGr,aireSecoMolSI\n",
    "    tablaIndex = TemperaturaSI(TK).copy()\n",
    "    tablaIndex.loc[:,listConvGr]/=aireSecoMol\n",
    "    tablaIndex = tablaIndex.rename(dictGr,axis=1)\n",
    "#Explicado en def TemperaturaINGLb(TR)\n",
    "        \n",
    "    return tablaIndex"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 20,
   "id": "79d1e01f",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Valores termodinámicos en función de Cp SI\n",
    "def CpSI(CP):\n",
    "    \"\"\"Valores termodinámicos en función de Cp SI\n",
    "    CP = Capacidad calorifica en (kJ/kmol*K)\"\"\"\n",
    "    global aireSIcp\n",
    "    aireSIcp,tablaIndex = TablaTermodinamica(aireSIcp,CP,cp=1)\n",
    "    return tablaIndex\n",
    "#Explicado en def TemperaturaING(TR)\n",
    "\n",
    "def CpSIKg(CP):\n",
    "    global dictGr\n",
    "    \"\"\"Valores termodinamicos en función de Cp SI, kg en lugar de mol\n",
    "    CP = Capacidad calorifica en (kJ/kg*K)\"\"\"\n",
    "    global dictLb,listConvLb,aireSecoMolING\n",
    "    CP=CP*aireSecoMol\n",
    "    tablaIndex = CpSI(CP).copy()\n",
    "    tablaIndex = tablaIndex.set_axis(['Temperatura(K)','h(kJ/kg)','s(kJ/kg*R)','Pr'])\n",
    "    tablaIndex.loc[['h(kJ/kg)','s(kJ/kg*R)']] /= aireSecoMol\n",
    "    return tablaIndex\n",
    "    #Explicado en def CpINGLb(CP)\n",
    "    "
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 21,
   "id": "056e26e9",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Valores termodinámicos en función de entalpia (h) SI\n",
    "def EntalpiaSI(H):\n",
    "    \"\"\"Valores termodinámicos en función de entalpía(h) SI\n",
    "    H = entalpía (kJ/kmol)\"\"\"\n",
    "    global aireSIh\n",
    "    aireSIh, tablaIndex = TablaTermodinamica(aireSIh,H)\n",
    "    return tablaIndex\n",
    "#Explicado en def TemperaturaING(TR)\n",
    "\n",
    "def EntalpiaSIKg(H):\n",
    "    global dictGr\n",
    "    \"\"\"Valores termodinamicos en función de entalpía(h) SI, kg en lugar de mol\n",
    "    H = entalpía (kJ/kg)\"\"\"\n",
    "    global dictLb\n",
    "    H=H*aireSecoMol\n",
    "    tablaIndex = EntalpiaSI(H).copy()\n",
    "    tablaIndex.reset_index(inplace=True)\n",
    "    tablaIndex.loc[:,listConvGr]/=aireSecoMol\n",
    "    tablaIndex = tablaIndex.rename(dictGr,axis=1)\n",
    "    tablaIndex.set_index('h(kJ/kg)',inplace=True)\n",
    "    return tablaIndex\n",
    "    #Explicado en def TemperaturaINGLb(TR) y EntalpiaINGLb(H)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 22,
   "id": "e9ce2217",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Valores termodinámicos en función de entropia (s) SI\n",
    "def EntropiaSI(S):\n",
    "    \"\"\"Valores termodinámicos en función de entropia(s) SI\n",
    "    S = entropía (kJ/kmol*K)\"\"\"\n",
    "    global aireSIs\n",
    "    aireSIs, tablaIndex = TablaTermodinamica(aireSIs,S)\n",
    "    return tablaIndex\n",
    "#Explicado en def TemperaturaING(TR)\n",
    "\n",
    "def EntropiaSIKg(S):\n",
    "    global dictGr\n",
    "    \"\"\"Valores termodinámicos en función de entropia(s) SI, kg en lugar de mol\n",
    "    S = entropía (kJ/kg*K)\"\"\"\n",
    "    global dictLb\n",
    "    S=S*aireSecoMol\n",
    "    tablaIndex = EntropiaSI(S).copy()\n",
    "    tablaIndex.reset_index(inplace=True)\n",
    "    tablaIndex.loc[:,listConvGr]/=aireSecoMol\n",
    "    tablaIndex = tablaIndex.rename(dictGr,axis=1)\n",
    "    tablaIndex.set_index('s(kJ/kg*K)',inplace=True)\n",
    "    return tablaIndex\n",
    "#Explicado en def TemperaturaINGLb(TR) y EntalpiaINGLb(H)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 23,
   "id": "477663e8",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Valores termodinámicos en función de su presion relativa (Pr) SI\n",
    "def PresionRelSI(PR):\n",
    "    \"\"\"Valores termodinámicos en función de su presión relativa(Pr) inglesas\n",
    "    PR = presión relativa\"\"\"\n",
    "    global aireSIpr\n",
    "    aireSIpr, tablaIndex = TablaTermodinamica(aireSIpr,PR)\n",
    "    return tablaIndex\n",
    "#Explicado en def TemperaturaING(TR)\n",
    "\n",
    "def PresionRelSIKg(PR):\n",
    "    global dictGr\n",
    "    \"\"\"Valores termodinámicos en función de su presión relativa(Pr) inglesas, kg en lugar de mol\n",
    "    PR = presión relativa\"\"\"\n",
    "    global dictLb\n",
    "    tablaIndex = PresionRelSI(PR).copy()\n",
    "    tablaIndex.loc[:,listConvGr]/=aireSecoMol\n",
    "    tablaIndex = tablaIndex.rename(dictGr,axis=1)\n",
    "    return tablaIndex\n",
    "#Explicado en def TemperaturaINGLb(TR) y EntalpiaINGLb(H)"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "c2324742",
   "metadata": {},
   "source": [
    "### FIN DE FUNCIONES BASADOS EN EL SISTEMA INTERNACIONAL (SI) ----------------------------------------------------------"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "4b253fe3",
   "metadata": {},
   "source": [
    "## FIN DE FUNCIONES COMPLEMENTO ----------------------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "1fe3dc3b",
   "metadata": {},
   "source": [
    "## INTERPOLACIONES ----------------------------------------------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 24,
   "id": "27212b4e",
   "metadata": {},
   "outputs": [],
   "source": [
    "#TemperaturaING(3025)\n"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 25,
   "id": "2a0a1d2b",
   "metadata": {},
   "outputs": [],
   "source": [
    "#TemperaturaINGLb(3026.5)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 26,
   "id": "645e3d40",
   "metadata": {
    "scrolled": true
   },
   "outputs": [],
   "source": [
    "#TemperaturaSI(2005.5)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 27,
   "id": "ab5fb4fb",
   "metadata": {},
   "outputs": [],
   "source": [
    "#TemperaturaSIKg(4900)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 28,
   "id": "a92d46c1",
   "metadata": {},
   "outputs": [],
   "source": [
    "# CpING(7.25)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 29,
   "id": "a23a90fa",
   "metadata": {},
   "outputs": [],
   "source": [
    "# CpINGLb(0.25)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 30,
   "id": "785ed795",
   "metadata": {},
   "outputs": [],
   "source": [
    "# CpSI(36.2)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 31,
   "id": "f68de565",
   "metadata": {},
   "outputs": [],
   "source": [
    "# CpSIKg(1.25)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 32,
   "id": "90cf37a6",
   "metadata": {},
   "outputs": [],
   "source": [
    "# EntalpiaING(20160.2)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 33,
   "id": "20865ff7",
   "metadata": {},
   "outputs": [],
   "source": [
    "# EntalpiaINGLb(700)\n"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 34,
   "id": "c09ed238",
   "metadata": {
    "scrolled": true
   },
   "outputs": [],
   "source": [
    "# EntalpiaSI(56455)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 35,
   "id": "01870b3c",
   "metadata": {},
   "outputs": [],
   "source": [
    "# EntalpiaSIKg(1900)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 36,
   "id": "873db611",
   "metadata": {},
   "outputs": [],
   "source": [
    "# EntropiaING(62)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 37,
   "id": "06e901d2",
   "metadata": {},
   "outputs": [],
   "source": [
    "# EntropiaINGLb(2.14)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 38,
   "id": "97e762f7",
   "metadata": {},
   "outputs": [],
   "source": [
    "# EntropiaSI(200)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 39,
   "id": "56a598bf",
   "metadata": {},
   "outputs": [],
   "source": [
    "# EntropiaSIKg(8.78)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 40,
   "id": "cd706d72",
   "metadata": {},
   "outputs": [],
   "source": [
    "# PresionRelING(2387)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 41,
   "id": "a69e45f5",
   "metadata": {},
   "outputs": [],
   "source": [
    "# PresionRelINGLb(2331.7)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 42,
   "id": "a2633691",
   "metadata": {
    "scrolled": false
   },
   "outputs": [],
   "source": [
    "# PresionRelSI(5000)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 43,
   "id": "ca2bfb9d",
   "metadata": {},
   "outputs": [],
   "source": [
    "# PresionRelSIKg(37.575)"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "f3e7232f",
   "metadata": {},
   "source": [
    "## FIN DE INTERPOLACIONES -----------------------------------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "45370c15",
   "metadata": {},
   "source": [
    "## FUNCIONES PARA CP VARIABLES ------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 44,
   "id": "ee92a312",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Función para definir el trabajo del compresor\n",
    "def trabajoCompresor(h1,h2):\n",
    "    \"\"\"El trabajo de compresor es h2-h1\n",
    "    P.E\n",
    "    trabajoCompresor(51,21)\n",
    "    Puede ser con entalpía especifica/molar o entalpía total\"\"\"\n",
    "    return h2-h1\n",
    "\n",
    "#Función para definir el calor de entrada\n",
    "def calorEntrada(h2,h3):\n",
    "    \"\"\"El calor de entrada es h3-h2\n",
    "    P.E\n",
    "    calorEntrada(51,21)\n",
    "    Puede ser con entalpía especifica/molar o entalpía total\"\"\"\n",
    "    return h3-h2\n",
    "\n",
    "#Función para definir el trabjo de turbinas\n",
    "def trabajoTurbina(h3,h4):\n",
    "    \"\"\"El trabajo de turbina es h3-h4\n",
    "    P.E\n",
    "    trabajoTurbina(51,21)\n",
    "    Puede ser con entalpía especifica/molar o entalpía total\"\"\"\n",
    "    return h3-h4\n",
    "\n",
    "#Función para definir el calor de salida\n",
    "def calorSalida(h1,h4):\n",
    "    \"\"\"El calor de salida es h4-h1\n",
    "    P.E\n",
    "    calorSalida(51,21)\n",
    "    Puede ser con entalpía especifica/molar o entalpía total\"\"\"\n",
    "    return h4-h1\n",
    "\n",
    "#Función para definir el trabajo neto\n",
    "def trabajoNeto(h1=None,h2=None,h3=None,h4=None,trabTurbina=0,trabCompresor=0):\n",
    "    \"\"\"El trabajo neto se puede sacar de 2 formas\n",
    "    - Asignando todos los valores de entalpia(h1,h2,h3,h4)\n",
    "    - Asignando valores de trabajo de turbina y compresor\n",
    "    P.E\n",
    "    - trabajoNeto(15.4,12.5,15.7,18.6) son con los 4 valores de entalpia\n",
    "    - trabajoNeto(trabTurbina=150, trabCompresor=130)\n",
    "    Energías\n",
    "    - Puede ser con entalpía especifica/molar o entalpía total\n",
    "    - Pueden ser energía especifica/molar o energía total\"\"\"\n",
    "    \n",
    "    if trabTurbina and trabCompresor != 0:\n",
    "        return trabTurbina-trabCompresor\n",
    "    if (trabTurbina !=0 and trabCompresor==0) or (trabTurbina==0 and trabCompresor!=0):\n",
    "        raise Exception(\"La turbina o el compresor no se les agregó trabajo en los argumentos\")\n",
    "    if (h1 is None) or (h2 is None) or (h3 is None) or (h4 is None):\n",
    "        raise Exception(\"Falta una variable de entalpia\")\n",
    "    if h1 and h2 and h3 and h4 is not None:\n",
    "        return h3-h4-(h2-h1)\n",
    "    raise Exception(\"Los argumentos son invalidos\")\n",
    "\n",
    "#Función para definir la eficiencia térmica\n",
    "def eficienciaTermica(trabNeto,calEntrada):\n",
    "    \"\"\"La eficiencia térmica del ciclo es trabajoNeto/calorEntrada\n",
    "    Útil para Cp variable\n",
    "    Puede ser con energía especifica/molar o energía total\"\"\"\n",
    "    return trabNeto/calEntrada\n",
    "\n",
    "\n",
    "    \n",
    "    \n",
    "    "
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 45,
   "id": "e02e43b1",
   "metadata": {},
   "outputs": [],
   "source": [
    "def formulasRelacionPresiones ():\n",
    "    PR1,PR2,PR3,PR4,P1,P2,P3,P4,RP=sympy.symbols(\"Pr_1 Pr_2 Pr_3 Pr_4 P_1 P_2 P_3 P_4 r_p\",real=True)\n",
    "    eq1=sympy.Eq(PR2/PR1,P2/P1)\n",
    "    eq2=sympy.Eq(PR3/PR4,P3/P4)\n",
    "    eq3=sympy.Eq(PR2/PR1,RP)\n",
    "    eq4=sympy.Eq(PR3/PR4,RP)\n",
    "    eq5=sympy.Eq(RP,P2/P1)\n",
    "    eq6=sympy.Eq(RP,P3/P4)\n",
    "    \n",
    "    return list([eq1,eq2,eq3,eq4])"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 46,
   "id": "a3c35607",
   "metadata": {},
   "outputs": [
    {
     "data": {
      "image/png": "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\n",
      "text/latex": [
       "$\\displaystyle \\left[ \\frac{Pr_{2}}{Pr_{1}} = \\frac{P_{2}}{P_{1}}, \\  \\frac{Pr_{3}}{Pr_{4}} = \\frac{P_{3}}{P_{4}}, \\  \\frac{Pr_{2}}{Pr_{1}} = r_{p}, \\  \\frac{Pr_{3}}{Pr_{4}} = r_{p}\\right]$"
      ],
      "text/plain": [
       "⎡Pr₂   P₂  Pr₃   P₃  Pr₂       Pr₃     ⎤\n",
       "⎢─── = ──, ─── = ──, ─── = rₚ, ─── = rₚ⎥\n",
       "⎣Pr₁   P₁  Pr₄   P₄  Pr₁       Pr₄     ⎦"
      ]
     },
     "execution_count": 46,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "formulasRelacionPresiones()"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "33a0045b",
   "metadata": {},
   "source": [
    "## CICLO BÁSICO CON FRICCIÓN (AIRE ESTÁNDAR)----------------------------------------------------------"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 47,
   "id": "f67d39c4",
   "metadata": {},
   "outputs": [],
   "source": [
    "def eficienciaCompresor(eficCompresor,h1,h2i=None,h2r=None,):\n",
    "    \"\"\"Se entrega el valor de la entalpia 2 real del compresor o de la ideal\n",
    "    Se hace un despeje de h2r de la formula (h2i-h1)/(h2r-h1)\n",
    "    Si metes una entalpia real despejará la entalpia ideal\n",
    "    Si metes una entapia ideal despejará la entalpia real\"\"\"\n",
    "    H1,H2I,EFCOMP,H2R=sympy.symbols(\"h_1 h_2i n_comp h_2r\",real=True)\n",
    "    eC=sympy.Eq(EFCOMP,(H2I-H1)/(H2R-H1))\n",
    "    eC=eC.subs(H1,h1).subs(H2I,h2i).subs(EFCOMP,eficCompresor).subs(H2R,h2r)\n",
    "    h2roi=sympy.solve(eC)[0]\n",
    "    return float(h2roi)\n",
    "    \n",
    "\n",
    "    "
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 48,
   "id": "dd6681eb",
   "metadata": {},
   "outputs": [],
   "source": [
    "def eficienciaTurbina(eficTurbina,h3,h4i=None,h4r=None):\n",
    "    \"\"\"Se entrega el valor de la entalpía 4 real de la turbina o de la ideal\n",
    "    Se hace el despeje h2r de la formula (h3-h4r)/(h3-h4i)\n",
    "    Si metes una entalpia real despejará la entalpia ideal\n",
    "    Si metes una entalpia ideal despejará la entalpia real\n",
    "    ES PREFRERIBLE USAR LA FUNCIÓN eficienciaTurbinaGas ya que es mejor\"\"\"\n",
    "    H3,H4I,EFTURB,H4R=sympy.symbols(\"h_3 h_4i n_turb h_4r\",real=True)\n",
    "    eT=sympy.Eq(EFTURB,(H3-H4R)/(H3-H4I))\n",
    "    eT=eT.subs(H3,h3).subs(H4I,h4i).subs(EFTURB,eficTurbina).subs(H4R,h4r)\n",
    "    h4roi=sympy.solve(eT)[0]\n",
    "    return float(h4roi)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 49,
   "id": "ad0048ca",
   "metadata": {},
   "outputs": [],
   "source": [
    "def eficienciaTurbinaGas(eficTurbinaGas,h3,h4i=None,h4r=None):\n",
    "    \"\"\"Se entrega el valor de la entalpia 4 real de la turbina o de la ideal\n",
    "    Se hace el despeje h2r o h2i, depende del valor que se metió\n",
    "    La formula es (h3-h4r)/(h3-h4i)\n",
    "    Si metes una entalpia real despejará la entalpia ideal\n",
    "    Si metes una entalpia ideal despejará la entalpia real\"\"\"\n",
    "    H3,H4I,EFTURB,H4R=sympy.symbols(\"h_3 h_4i n_turb h_4r\", real=True)\n",
    "    eT=sympy.Eq(EFTURB,(H3-H4R)/(H3-H4I))\n",
    "    eT=eT.subs(H3,h3).subs(H4I,h4i).subs(EFTURB,eficTurbinaGas).subs(H4R,h4r)\n",
    "    h4roi=sympy.solve(eT)[0]\n",
    "    return float(h4roi)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 50,
   "id": "f7395644",
   "metadata": {},
   "outputs": [],
   "source": [
    "def eficienciaTurbinaPotencia(eficTurbinaPotencia,h4r,h5i=None,h5r=None):\n",
    "    \"\"\"Se entrega el valor de la entalpia 5 real de la turbina o de la ideal\n",
    "    Se hace el despeje h5r o h5i, depende del valor que se metió\n",
    "    La formula es (h4r-h5r)/(h4r-h5i)\n",
    "    Si metes una entalpia real despejará la entalpia ideal\n",
    "    SI metes una entalpia ideal despejará la entalpia real\"\"\"\n",
    "    H4R,H5I,EFTURB,H5R=sympy.symbols(\"h_4r h_5i n_turb h_5r\", real=True)\n",
    "    eT=sympy.Eq(EFTURB,(H4R-H5R)/(H4R-H5I))\n",
    "    eT=eT.subs(H4R,h4r).subs(H5I,h5i).subs(EFTURB,eficTurbinaPotencia).subs(H5R,h5r)\n",
    "    h4roi=sympy.solve(eT)[0]\n",
    "    return float(h4roi)\n",
    "    "
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 51,
   "id": "fecacfbc",
   "metadata": {},
   "outputs": [],
   "source": [
    "# eficienciaTurbinaGas(eficTurbinaGas=0.89,h3=35128.8,h4r=25193.2457597701)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 52,
   "id": "11740872",
   "metadata": {
    "scrolled": true
   },
   "outputs": [],
   "source": [
    "# eficienciaTurbina(35128.8,23965.2559098541,0.89)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 53,
   "id": "018bbee8",
   "metadata": {},
   "outputs": [],
   "source": [
    "def formulasFriccion():\n",
    "    NT,NC,WTGR,WTGI,WTPR,WTPI,WCR,WCI=sympy.symbols(\"eta_t eta_c w_TGr w_TGi w_TPr w_TPi w_Cr w_Ci\", real=True)\n",
    "    H1,H2I,H3,H4I,H5I,H2R,H5R, H4R=sympy.symbols(\"h_1 h_2i h_3 h_4i h_5i h_2r h_5r h_4r\", real=True)\n",
    "    PR1,PR2I,PR2R,PR3,PR4I,PR4R,PR5I,PR5R,RP=sympy.symbols(\"p_r1 p_r2i p_r2r p_r3 p_r4i p_r4r p_r5i p_r5r r_p\",real=True)\n",
    "    eq1=sympy.Eq(NC,WCI/WCR)\n",
    "    eq2=sympy.Eq(NC,(H2I-H1)/(H2R-H1))\n",
    "    eq3=sympy.Eq(NT,WTGR/WTGI)\n",
    "    eq4=sympy.Eq(NT,(H3-H4R)/(H3-H4I))\n",
    "    eq5=sympy.Eq(NT,WTPR/WTPI)\n",
    "    eq6=sympy.Eq(NT,(H4R-H5R)/(H4R-H5I))\n",
    "    \n",
    "    return list([eq1,eq2,eq3,eq4,eq5,eq6])\n",
    "    "
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 54,
   "id": "46944f0a",
   "metadata": {},
   "outputs": [],
   "source": [
    "def formulasFriccionPresiones():\n",
    "    PR1,PR2I,PR2R,PR3,PR4I,PR4R,PR5I,PR5R,RP=sympy.symbols(\"p_r1 p_r2i p_r2r p_r3 p_r4i p_r4r p_r5i p_r5r r_p\",real=True)\n",
    "    P1,P2,P3,P4,P5=sympy.symbols(\"p_1 p_2 p_3 p_4 p_5\")\n",
    "    eq1=sympy.Eq(RP, PR2I/PR1)\n",
    "    eq2=sympy.Eq(P2/P1,PR2I/PR1)\n",
    "    eq3=sympy.Eq(P3/P4,PR3/PR4I)\n",
    "    eq4=sympy.Eq(P4/P5,PR4R/PR5I)\n",
    "    \n",
    "    return list([eq1,eq2,eq3,eq4])"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 55,
   "id": "25f82830",
   "metadata": {},
   "outputs": [],
   "source": [
    "# formulasFriccionPresiones()"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "d4a37bff",
   "metadata": {},
   "source": [
    "## FIN CICLO BÁSICO CON FRICCIÓN (AIRE ESTÁNDAR) ---------------------------------------------------"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 56,
   "id": "7f0ca814",
   "metadata": {},
   "outputs": [],
   "source": [
    "# PR1,PR2,PR3,PR4,P1,P2,P3,P4,RP=sympy.symbols(\"Pr_1 Pr_2 Pr_3 Pr_4 P_1 P_2 P_3 P_4 r_p\",real=True)\n",
    "# eq1=sympy.Eq(PR2/PR1,P2/P1)\n",
    "# eq2=sympy.Eq(PR3/PR4,P3/P4)\n",
    "# eq3=sympy.Eq(PR2/PR1,RP)\n",
    "# eq4=sympy.Eq(PR3/PR4,RP)\n",
    "# eq3=eq3.subs(RP,15.88).subs(PR2,19.20686).subs(PR3,None)\n",
    "# sympy.solve(eq3)[0]\n",
    "\n",
    "# # list([eq1,eq2])"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 57,
   "id": "e632b069",
   "metadata": {},
   "outputs": [],
   "source": [
    "def gasesIdeales():\n",
    "    empty"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "7fe1826c",
   "metadata": {},
   "source": [
    "## FIN DE FUNCIONES PARA CP VARIABLES ---------------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "7de9b326",
   "metadata": {},
   "source": [
    "## VALORES PARA CP CONSTANTE ---------------------------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 58,
   "id": "de0304a0",
   "metadata": {},
   "outputs": [],
   "source": [
    "# LAS MISMAS FUNCIONES QUE LAS DE ARRIBA PERO PARA CP CONSTANTES\n",
    "def trabajoCompresorCpCon(T1,T2,cp):\n",
    "    \"\"\"El trabajo de compresor es cp(T2-T1)\n",
    "    \n",
    "    Unidades\n",
    "    Si CP[=]kJ/kg*K entonces T1 [=]K, T2[=]K y la función entrega energía especifica[=]kJ/kg\n",
    "    Si CP[=]BTU/lb*R entonces T1[=]R, T2[=]R y la función entrega energía especifica[=]BTU/lb\n",
    "    \n",
    "    Si CP[=]kJ/kmol*K entonces T1[=]K, T2[=]K y la función entrega energía especifica[=]kJ/kmol\n",
    "    Si CP[=]BTU/mol*K entonces T1[=]K, T2[=]K y la función entrega energía especifica[=]BTU/mol\"\"\"\n",
    "    return cp*(T2-T1)\n",
    "\n",
    "def calorEntradaCpCon(T2,T3,cp):\n",
    "    \"\"\"El calor de entrada es cp(T3-T2)\n",
    "    \n",
    "    Unidades\n",
    "    Si CP[=]kJ/kg*K entonces T1 [=]K, T2[=]K y la función entrega energía especifica[=]kJ/kg\n",
    "    Si CP[=]BTU/lb*R entonces T1[=]R, T2[=]R y la función entrega energía especifica[=]BTU/lb\n",
    "    \n",
    "    Si CP[=]kJ/kmol*K entonces T1[=]K, T2[=]K y la función entrega energía especifica[=]kJ/kmol\n",
    "    Si CP[=]BTU/mol*K entonces T1[=]K, T2[=]K y la función entrega energía especifica[=]BTU/mol\"\"\"\n",
    "    return cp*(T3-T2)\n",
    "    \n",
    "def trabajoTurbinaCpCon(T3,T4,cp):\n",
    "    \"\"\"El trabajo de turbina es cp(T3-T4)\n",
    "    \n",
    "    Unidades\n",
    "    Si CP[=]kJ/kg*K entonces T1 [=]K, T2[=]K y la función entrega energía especifica[=]kJ/kg\n",
    "    Si CP[=]BTU/lb*R entonces T1[=]R, T2[=]R y la función entrega energía especifica[=]BTU/lb\n",
    "    \n",
    "    Si CP[=]kJ/kmol*K entonces T1[=]K, T2[=]K y la función entrega energía especifica[=]kJ/kmol\n",
    "    Si CP[=]BTU/mol*K entonces T1[=]K, T2[=]K y la función entrega energía especifica[=]BTU/mol\"\"\"\n",
    "    return cp*(T3-T4)\n",
    "\n",
    "def calorSalidaCpCon(T1,T4,cp):\n",
    "    \"\"\"El calor de salida es cp(T4-T1)\n",
    "    \n",
    "    Unidades\n",
    "    Si CP[=]kJ/kg*K entonces T1 [=]K, T2[=]K y la función entrega energía especifica[=]kJ/kg\n",
    "    Si CP[=]BTU/lb*R entonces T1[=]R, T2[=]R y la función entrega energía especifica[=]BTU/lb\n",
    "    \n",
    "    Si CP[=]kJ/kmol*K entonces T1[=]K, T2[=]K y la función entrega energía especifica[=]kJ/kmol\n",
    "    Si CP[=]BTU/mol*K entonces T1[=]K, T2[=]K y la función entrega energía especifica[=]BTU/mol\"\"\"\n",
    "    return cp*(T4-T1)\n",
    "\n",
    "def trabajoNetoCpCon(T1,T2,T3,cp,T4=None):\n",
    "    \"\"\"El trabajo neto\n",
    "    No es necesario tener un valor de T4, con las 3 temperaturas se puede realizar\n",
    "    Si detecta un valor de T4 utilizará la formula convencional con todas las temperaturas involucradas\n",
    "    \n",
    "    Unidades\n",
    "    Si CP[=]kJ/kg*K entonces T1 [=]K, T2[=]K y la función entrega energía especifica[=]kJ/kg\n",
    "    Si CP[=]BTU/lb*R entonces T1[=]R, T2[=]R y la función entrega energía especifica[=]BTU/lb\n",
    "    \n",
    "    Si CP[=]kJ/kmol*K entonces T1[=]K, T2[=]K y la función entrega energía especifica[=]kJ/kmol\n",
    "    Si CP[=]BTU/mol*K entonces T1[=]K, T2[=]K y la función entrega energía especifica[=]BTU/mol\"\"\"\n",
    "    if T4 is None:\n",
    "        return cp*(T3+T1-T2-(T3*T1/T2))\n",
    "    if T4 is not None:\n",
    "        return cp*(T3+T1-T2-T4)\n",
    "\n",
    "def temperatura2TrabMax(T1,T3):\n",
    "    \"\"\"Temperatura 2 para trabajo máximo\n",
    "    \n",
    "    Unidades\n",
    "    Si T1[=]K entonces T3[=]K o viceversa\n",
    "    Si T1[=]R entonces T3[=]R o viceversa\n",
    "    La función entrega un valor de temperatura\"\"\"\n",
    "    return (T1*T3)**(1/2)\n",
    "\n",
    "def temperatura4(T1,T2,T3):\n",
    "    \"\"\"Temperatura 4\n",
    "    \n",
    "    Unidades\n",
    "    T1[=]T2[=]T3[=]K\n",
    "    T1[=]T2[=]T3[=]R\"\"\"\n",
    "    return (T3*T1)/T2\n",
    "    \n",
    "def eficienciaTermicaCpCon(T1,T2,T3,T4):\n",
    "    \"\"\"La eficiencia térmica del ciclo es\n",
    "    1-(T4-T1)/(T3-T2)\n",
    "    Útil para Cp constante\n",
    "    \n",
    "    Unidades\n",
    "    T1[=]T2[=]T3[=]T4[=]K\n",
    "    ó\n",
    "    T1[=]T2[=]T3[=]T4[=]R\"\"\"\n",
    "    return (1-(T4-T1)/(T3-T2))\n"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "c3b92d6b",
   "metadata": {},
   "source": [
    "\n",
    "## FIN DE VALORES PARA CP CONSTANTE -----------------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "7a9c71f8",
   "metadata": {},
   "source": [
    "## ECUACIONES PARA CP VARIABLE -------------------------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 59,
   "id": "c4458a4d",
   "metadata": {},
   "outputs": [],
   "source": [
    "def presionRelativa(pr1=None,pr2=None,pr3=None,pr4=None,p1=None,p2=None,p3=None,p4=None,rp=None):\n",
    "    \"\"\"La presión relativa no tiene unidades\n",
    "    Pero se tiene que tener en cuenta que la división de presiones cancele estas unidades\n",
    "    Se puede meter la relación de presiones en lugar de la división de presiones\n",
    "    P.E.\n",
    "    presionRelativa(pr1=15,rp=5) --> Daría la presión relativa 2\n",
    "    presionRelativa(pr2=15,rp=5) --> Daría la presión relativa 1\n",
    "    presionRelativa(pr3=10,rp=2) --> Daría la presión relativa 4\n",
    "    presionRelativa(pr4=5, rp=6) --> Daría la presión relativa 3\n",
    "    \n",
    "    presionRelativa(pr1=15,p1=2,p2=10) --> Daría la presion relativa 2\n",
    "    presionRelativa(pr2=15,p1=2,p2=10) --> Daría la presión relativa 1\n",
    "    presionRelativa(pr1=15,p3=2,p4=10) --> Daría la presión relativa 2\n",
    "    \n",
    "    En conclusión, si se tienen los valores necesarios, se puede conseguir una presión relativa con las presiones que se tengan\n",
    "    Hay que tener cuidado de no meter dos valores de presion relativa\n",
    "    \"\"\"\n",
    "    PR1,PR2,PR3,PR4,P1,P2,P3,P4,RP=sympy.symbols(\"Pr_1 Pr_2 Pr_3 Pr_4 P_1 P_2 P_3 P_4 r_p\",real=True)\n",
    "    if (rp is not None) and ((pr1 is not None) or (pr2 is not None)):\n",
    "        #Se puede sacar pr1 o pr2\n",
    "        eq1=sympy.Eq(PR2/PR1,RP)\n",
    "        eq1=eq1.subs(RP,rp).subs(PR1,pr1).subs(PR2,pr2)\n",
    "        return float(sympy.solve(eq1)[0])\n",
    "    \n",
    "    if (rp is not None) and ((pr3 is not None) or (pr4 is not None)):\n",
    "        #Se puede sacar pr3 o pr4\n",
    "        eq2=sympy.Eq(PR3/PR4,RP)\n",
    "        eq2=eq2.subs(RP,rp).subs(PR3,pr3).subs(PR4,pr4)\n",
    "        return float(sympy.solve(eq2)[0])\n",
    "    \n",
    "    if (p1 is None):\n",
    "        p1=p4\n",
    "    if (p2 is None):\n",
    "        p2=p3\n",
    "    if (p1 is not None) and (p2 is not None) and ((pr1 is not None) or (pr2 is not None)):\n",
    "        #Se puede sacar pr1 o pr2\n",
    "        eq3=sympy.Eq(PR2/PR1,P2/P1)\n",
    "        eq3=eq3.subs(P1,p1).subs(P2,p2).subs(PR2,pr2).subs(PR1,pr1)\n",
    "        return float(sympy.solve(eq3)[0])\n",
    "    \n",
    "    if (p3 is None):\n",
    "        p3=p2\n",
    "    if (p4 is None):\n",
    "        p4=p1\n",
    "    if (p3 is not None) and (p4 is not None) and ((pr3 is not None) or(pr4 is not None)):\n",
    "        #Se puede sacar pr3 o pr4\n",
    "        eq4=sympy.Eq(PR3/PR4,P3/P4)\n",
    "        eq4=eq4.subs(PR3,pr3).subs(PR4,pr4).subs(P3,p3).subs(P4,p4)\n",
    "        return float(sympy.solve(eq4)[0])\n",
    "    \n",
    "    raise Exception(\"Alguno de los valores está incorrecto\")\n",
    "        \n",
    "        \n",
    "    \"\"\"if ((p1 is not None) and (p2 is not None)) or ((p3 is not None) and (p4 is not None)):\n",
    "        \n",
    "    \n",
    "    \n",
    "    if (p1 is not None) and (p2 is not None) and (pr1 is not None):\n",
    "        #Entonces se puede sacar pr2\n",
    "        eq1=sympy.Eq(PR2/PR1,P2/P1)\n",
    "        return\n",
    "    if (p1 is not None) and (p2 is not None) and (pr2 is not None):\n",
    "        #Se puede sacar pr1\n",
    "        eq1=sympy.Eq(PR2/PR1,P2/P1)\n",
    "        return\n",
    "    if (p3 is not None) and (p4 is not None) and (pr3 is not None):\n",
    "        #Se puede sacar pr4\n",
    "        \n",
    "        return\n",
    "    if (p3 is not None) and (p4 is not None) and (pr4 is not None):\n",
    "        #Se puede sacar pr3\n",
    "        return\n",
    "    if (rp is not None) and ()\n",
    "    \"\"\""
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 60,
   "id": "fc6a9d64",
   "metadata": {},
   "outputs": [
    {
     "data": {
      "image/png": "iVBORw0KGgoAAAANSUhEUgAAAMQAAAAQCAYAAABJCdBSAAAAOXRFWHRTb2Z0d2FyZQBNYXRwbG90bGliIHZlcnNpb24zLjcuMCwgaHR0cHM6Ly9tYXRwbG90bGliLm9yZy88F64QAAAACXBIWXMAABJ0AAASdAHeZh94AAAFjUlEQVR4nO2aa4hVVRTHf6MmTuKbJKgoHSzLkSRSG8tXmj2EUNM+hKYFmWSNZoKQ2uJfBPbBMsPoJZoQpBVE6violIy0AsMoLbVMyMjCV5hJpWMf1j52PHPu3DlnhvvhMn+47HP23v+1176sdfbaa++Kc+fO0YpWtMLRLnqQNA1YUaR/vZm1jXEmAsOBAcD1QCfgLTObXGxgSUOB2cAQoDtwDPgGWGJmdSn9LweeBu4AegC/Au8DMrPjTRivBzAeGAv0By4D/gljrgBWmFl9glMBPABMB/oBbYG9of8yMzvbHPnNmVspOOWiVxY7bRN73gWowG9L6LMhwV8APBoG+iVtsmmQtADYBgwDNgKLgbVAN2BESv8qYCdunF8CLwAHgFnAjmCMxTAJeB0YDHwBLAHeA6qBN4A1wQHieBNYDvQCVgd+e+BFYHWifx75ueZWCk456UUGOz2/QpjZLtwpGkDSjvD4WqLpceAQ8APugVsbGyzImgQ8A3wETDCzk4n2i1JoLwM9gVozeynW9/mgw7PAjCJD7wPuBtbHv9SSnsT/2HuACbgRI2kcMAX4CRhkZkdi+q0J/acCK/PIb+bcSsEpJ72abKdtCjXEBqoGbsI9a328zcy2mtl+M2vSRkRSG+A54C/gvqQzBJn/Jji9gTHAQWBZsjtwCpgiqWNjY5vZFjNbmwxbzOww8Ep4HRFrmhDKxZEzxPRbGF4fa4b8XHMrBaec9IJsdlrUIYCHQ7k8HjPnxBA8/KgDjksaK2mepFmSagpwbg3l5hRjOwl8BlyMO21eRE54JlZ3aSgPpPSP6m6Q1DWnfMg3t1JwykmvTGjUISRVApOBejwObi4GhvI34CtgHbAIj7e3S/pE0iUJzjWh3FdA5v5QXp1HIUntgPvD68ZYU7Qq9Eqh9Y49980pH/LNrRScctIrE4qtEPcCXYENZvZz3kFi6BnKGUAlMBrf8VcDm/BN9jsJTpdQ/lFAZlTfNadOi8L4dWa2KVa/LpRzJHWPKoOBK9avW075kG9upeCUk16Z0K5I+/RQvpp3gASilG0FMNHMvg7vuyWNxz1/uKQaM9uRKqEhosxN5gMVSbXAE8D3+AY6jrfx1fFOYI+kD/C9z2igCv8a9QEKhpFF5DcFeeZWCk456XUBCq4Qkq7DY/5DeMzfEohyxAdizgCAmZ3GVwmAQbGmyOu7kI7OiX5NgqSZePp0DzDSzI4l9KnHs0ZzgcO4QT+I/x+3AEdD19/zyE/onGVupeCUk16Z0NgK0ZKb6Qh7Q3miQHvkMJUpnEJxYZ9QFoorG0DSbDx//S0wysxSjdrMzuBnJIsT/Eo8p30a2J1XPvnmVgpOOemVCakrhKQO+BexHj+YailswzMtfSS1T2mvDuXBWF2UMx4T0rZxPTsBN+OG+XlTFJA0DzfWXfiXu5CxNoYpQAdgTUqaOIv8PHMrBaec9MqEQiHTJHyzWNdCm2kAQj5/Nb7kPRVvk3QbcDu+3G2McX4ENgNXATMTIgV0BFaZ2amYrCpJfZOHfJIW4pvcnfiX+wiNQFLnlLqBQcaf+PWB3PLzzK0UnHLSKysKhUzRZjp5Mn2hBn6aOy68Rnn7Gkkrw/MRM5uboM3BrzfMlzQMP8W9Er8HdBZ4yMxOJDiPANuBpZJGAd8FGSPx5XF+ov/HQWYvwmojaSpuwGeBT4FaSQkaB81sZez9Q0mn8dDnJH6f6S7gb/yU/fwZRU75eeZWKk7Z6JXFThusEJKuxTeNTdlMD8CvL0zFv+7gOfqobmKSEEKIwXhYcQVQix+4rAeGmlky7Rp9GW7Er0kMxjM3VcBSoMbMjiY5KYjOE9rilwot5TctwXkXTwtPxh25P34e0y8lhZpHfq65lYJTTnqRwU4rWq9/t6IV/+M/U9oAol+MPf8AAAAASUVORK5CYII=\n",
      "text/latex": [
       "$\\displaystyle 7160.29200000001$"
      ],
      "text/plain": [
       "7160.292000000011"
      ]
     },
     "execution_count": 60,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "presionRelativa(p4=2,p3=31.76,pr4=450.9)"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "fe206dc4",
   "metadata": {},
   "source": [
    "## ECUACIONES PARA CP VARIABLE -------------------------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "ff7a3817",
   "metadata": {},
   "source": [
    "## ECUACIONES PARA CP CONSTANTE ----------------------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 61,
   "id": "9b2e47e7",
   "metadata": {},
   "outputs": [],
   "source": [
    "# import sympy\n",
    "\n"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 62,
   "id": "73ae0364",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Función para sacar T1 ó T2 con la relación de presiones y la relación de capacidades calorificas\n",
    "def temperaturaRelacion12(k,t1=None,t2=None,r=None,p1=None,p2=None):\n",
    "    \"\"\"Función para sacar T1 ó T2 con la relación de presiones y la relación de capacidades calorificas\"\"\"\n",
    "    T1,T2,R,P1,P2,K=sympy.symbols('T_1 T_2 r_p P_1 P_2 k',real=True)\n",
    "    eq1=sympy.Eq(P2/P1,(T2/T1)**(k/(k-1)))\n",
    "    eq2=sympy.Eq(R,(T2/T1)**(k/(k-1)))\n",
    "    if (t1 is not None)and(p1 is not None)and(p2 is not None):\n",
    "        #Significa que se despejará T2 con las presiones p1 y p2\n",
    "        eq1=eq1.subs(T1,t1).subs(P1,p1).subs(P2,p2).subs(K,k)\n",
    "        Temp2=sympy.solve(eq1,T2)[0]\n",
    "        return Temp2\n",
    "        \n",
    "        \n",
    "    if (t2 is not None)and(p1 is not None)and(p2 is not None):\n",
    "        #Significa que se despejará T1 con las presiones p1 y p2\n",
    "        eq1=eq1.subs(T2,t2).subs(P1,p1).subs(P2,p2).subs(K,k)\n",
    "        Temp1=sympy.solve(eq1,T1)[0]\n",
    "        return Temp1\n",
    "        \n",
    "    if (t1 is not None)and(r is not None):\n",
    "        #Significa que se despejará T2 con r\n",
    "        eq2=eq2.subs(T1,t1).subs(R,r).subs(K,k)\n",
    "        Temp2=sympy.solve(eq2,T2)[0]\n",
    "        return Temp2\n",
    "        \n",
    "        \n",
    "    if (t2 is not None)and(r is not None):\n",
    "        #Significa que se despejará T1 con r\n",
    "        eq2=eq2.subs(T2,t2).subs(R,r).subs(K,k)\n",
    "        Temp2=sympy.solve(eq2,T1)[0]\n",
    "        return Temp2\n",
    "        \n",
    "        \n",
    "    if ((p1 is not None)and(p2 is None))or((p1 is None)and(p2 is not None)):\n",
    "        raise Exception(\"Hace falta una presión\")\n",
    "\n",
    "    raise Exception(\"Alguno de los parametros no hace sentido\")\n",
    "    "
   ]
  },
  {
   "cell_type": "markdown",
   "id": "4e49be9e",
   "metadata": {},
   "source": [
    "## FIN DE ECUACIONES PARA CP CONSTANTE -----------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "f14b82df",
   "metadata": {},
   "source": [
    "# COMBUSTIÓN ------------------------------------------------------------------------------------------\n",
    "los combustibles utilizados en las turbinas de gas son por\n",
    "lo general hidrocarburos, cuya fórmula general es CxHy"
   ]
  },
  {
   "attachments": {
    "image.png": {
     "image/png": 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"
    }
   },
   "cell_type": "markdown",
   "id": "f127400b",
   "metadata": {},
   "source": [
    "HIDROCARBURO\n",
    "![image.png](attachment:image.png)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 63,
   "id": "54bf7171",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Aire seco teoricamente requerido\n",
    "def aireSecoCombustion(X,Y):\n",
    "    \"\"\"La cantidad de aire seco teóricamente requerido para la reacción dada en la ecuación\n",
    "    X y Y provienen de \n",
    "    CxHy + (x+y/4)O2 -> xCO2+y/2*H2O\"\"\"\n",
    "    T,x,y=sympy.symbols(\"T x y\",real=True)\n",
    "    eq=sympy.Eq(T,(x+y/4)/0.2095)\n",
    "    eq=eq.subs(x,X).subs(y,Y)\n",
    "    sol=sympy.solve(eq)[0]\n",
    "    return sol"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 64,
   "id": "3fa17708",
   "metadata": {},
   "outputs": [],
   "source": [
    "def excesoAire(porcExceso=None,suministradaReal=None,suministradaTeorica=None):\n",
    "    \"\"\"La función despejará y entregará el valor de la variable que no sea dada, puede ser el porcentaje de exceso\n",
    "    Los moles suministrados reales o los moles suministrados teoricos\n",
    "    Los moles deben ser ingresados en valores numericos. PE. porcExceso = 40 para 40%\n",
    "    %excAire=(s-r)/r*100\n",
    "    porcExceso --> %excAire\n",
    "    suministradaReal --> s   -->moles\n",
    "    suministradaTeorica --> r ->moles\n",
    "    Deben haber 2 parametros para que el tercero que no se ingresó sea el despejado y entregado por la función\n",
    "    sino se ingresa ningun parametro se imprime en la pantalla la ecuación seguida\"\"\"\n",
    "    XAS, S, R=sympy.symbols(\"X_as S R'\",real=True)\n",
    "    eq=sympy.Eq(XAS,(S-R)/R*100)\n",
    "    if porcExceso==None and suministradaReal==None and suministradaTeorica==None:\n",
    "        return eq\n",
    "    eq=eq.subs(XAS,porcExceso).subs(S,suministradaReal).subs(R,suministradaTeorica)\n",
    "    sol=sympy.solve(eq)[0]\n",
    "    \n",
    "        \n",
    "    return sol\n",
    "    "
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 65,
   "id": "248a3a47",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Reacción general\n",
    "def reaccionGeneral(X,Y=None,porcExcAire=None):\n",
    "    \"\"\"Si es alcano entonces solamente meter el valor de X, si no lo es entonces meter el valor de Y también\n",
    "    Escribir el porcentaje de exceso de aire. PE porcExcAire=40 sería para 40%\"\"\"\n",
    "    x=X\n",
    "    y=Y\n",
    "    if Y is None:\n",
    "        y=2*x+2\n",
    "    if Y is not None:\n",
    "        y=Y\n",
    "    aireSecoCombustible=round(float(aireSecoCombustion(x,y)),ndigits=4)\n",
    "    if porcExcAire is not None:\n",
    "        aireSecoCombustible=round(excesoAire(porcExceso=porcExcAire,suministradaTeorica=aireSecoCombustible),ndigits=4)\n",
    "        print(aireSecoCombustible)\n",
    "    s1=\"C\"\n",
    "    s2=\"H\"\n",
    "    s3=\" O2\"\n",
    "    s4=\" CO2\"\n",
    "    s5=\" H2O\"\n",
    "    S1=\"La reacción general es\"\n",
    "    S2=\"La reacción con aire seco es\"\n",
    "    s6=str(aireSecoCombustible)+\" AS\"\n",
    "    CnHm=s1+str(x)+s2+str(y)\n",
    "    print(S1)\n",
    "    print(s1+str(x)+s2+str(y)+\" + \"+str(round(x+y/4,ndigits=1))+s3+\" --> \"+str(x)+s4+\" + \"+str(round(y/2,ndigits=1))+s5)\n",
    "    \n",
    "    print(S2)\n",
    "    \n",
    "    print(CnHm+\" + \"+s6+\" --> \"+str(x)+s4+\" + \"+str(round(y/2,ndigits=1))+s5+\" + \"+s6 +str(round(-(x+y/4),ndigits=1))+s3)\n",
    "    \n",
    "    #Valor de moles reacción general\n",
    "    molCnHm=1\n",
    "    molO2=-round(x+y/4,ndigits=1)\n",
    "    molCO2=x\n",
    "    molH2O=round(y/2,ndigits=1)\n",
    "    #Valor de mol aire seco\n",
    "    molAireSeco=aireSecoCombustible\n",
    "    print(\"\\n\\nLos moles para la reacción con aire seco\")\n",
    "    print(\"\")\n",
    "    print(CnHm+\"\\t\"+str(molCnHm))\n",
    "    print(s3+\"\\t\"+str(molO2))\n",
    "    print(s4+\"\\t\"+str(molCO2))\n",
    "    print(s5+\"\\t\"+str(molH2O))\n",
    "    print(\"Aire\"+\"\\t\"+str(molAireSeco))\n",
    "    "
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 66,
   "id": "5216331b",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Tener los datos de la tabla de excel\n",
    "tablaCompuestosExcel=pd.ExcelFile(\"Tablasdecompuestos.xlsx\")\n",
    "CO2_SI=pd.read_excel(tablaCompuestosExcel,sheet_name=0)\n",
    "CO2_ING=pd.read_excel(tablaCompuestosExcel,sheet_name=1)\n",
    "H2O_SI=pd.read_excel(tablaCompuestosExcel,sheet_name=2)\n",
    "H2O_ING=pd.read_excel(tablaCompuestosExcel,sheet_name=3)\n",
    "CAL_FORM=pd.read_excel(tablaCompuestosExcel,sheet_name=4)\n",
    "O2_ING=pd.read_excel(tablaCompuestosExcel,sheet_name=5)\n",
    "O2_SI=pd.read_excel(tablaCompuestosExcel,sheet_name=6)\n",
    "TABLA_K=pd.read_excel(tablaCompuestosExcel,sheet_name=7) # UTIL EN TURBINAS DE GAS PARA LA PROPULSIÓN DE AERONAVES\n",
    "ISA_ING=pd.read_excel(tablaCompuestosExcel,sheet_name=8) # UTIL EN TURBINAS DE GAS PARA LA PROPULSIÓN DE AERONAVES\n",
    "ISA_SI=pd.read_excel(tablaCompuestosExcel,sheet_name=9) # UTIL EN TURBINAS DE GAS PARA LA PROPULSIÓN DE AERONAVES"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 67,
   "id": "be4d2fa3",
   "metadata": {},
   "outputs": [],
   "source": [
    "#CELDA PARA TURBINAS DE GAS PARA LA PROPULSIÓN DE AERONAVES\n",
    "kTablaSI=TABLA_K.set_index(\"Temperatura (K)\").drop([\"Temperatura (R)\",\"k(R) \"],axis=1).dropna()\n",
    "kTablaING=TABLA_K.set_index(\"Temperatura (R)\").drop([\"Temperatura (K)\", \"k(K)\"],axis=1).dropna()\n",
    "altitudTablaING=ISA_ING.set_index(\"Altitud(ft)\")\n",
    "altitudTablaSI=ISA_SI.set_index(\"Altitud(m)\")"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 68,
   "id": "ec2ad8d5",
   "metadata": {},
   "outputs": [
    {
     "data": {
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       "    }\n",
       "\n",
       "    .dataframe thead th {\n",
       "        text-align: right;\n",
       "    }\n",
       "</style>\n",
       "<table border=\"1\" class=\"dataframe\">\n",
       "  <thead>\n",
       "    <tr style=\"text-align: right;\">\n",
       "      <th></th>\n",
       "      <th>k(R)</th>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>Temperatura (R)</th>\n",
       "      <th></th>\n",
       "    </tr>\n",
       "  </thead>\n",
       "  <tbody>\n",
       "    <tr>\n",
       "      <th>400</th>\n",
       "      <td>1.400</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>500</th>\n",
       "      <td>1.400</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>600</th>\n",
       "      <td>1.399</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>700</th>\n",
       "      <td>1.396</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>800</th>\n",
       "      <td>1.392</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>900</th>\n",
       "      <td>1.386</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1000</th>\n",
       "      <td>1.381</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1100</th>\n",
       "      <td>1.374</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1200</th>\n",
       "      <td>1.368</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1300</th>\n",
       "      <td>1.362</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1400</th>\n",
       "      <td>1.356</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1500</th>\n",
       "      <td>1.350</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1600</th>\n",
       "      <td>1.345</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1700</th>\n",
       "      <td>1.340</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1800</th>\n",
       "      <td>1.336</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1900</th>\n",
       "      <td>1.332</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2000</th>\n",
       "      <td>1.329</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2100</th>\n",
       "      <td>1.326</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2200</th>\n",
       "      <td>1.323</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2300</th>\n",
       "      <td>1.320</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2400</th>\n",
       "      <td>1.318</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2500</th>\n",
       "      <td>1.315</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2600</th>\n",
       "      <td>1.313</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2700</th>\n",
       "      <td>1.311</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2800</th>\n",
       "      <td>1.309</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2900</th>\n",
       "      <td>1.307</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>3000</th>\n",
       "      <td>1.306</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>3100</th>\n",
       "      <td>1.304</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>3200</th>\n",
       "      <td>1.303</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>3300</th>\n",
       "      <td>1.301</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>3400</th>\n",
       "      <td>1.300</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>3500</th>\n",
       "      <td>1.299</td>\n",
       "    </tr>\n",
       "  </tbody>\n",
       "</table>\n",
       "</div>"
      ],
      "text/plain": [
       "                 k(R) \n",
       "Temperatura (R)       \n",
       "400              1.400\n",
       "500              1.400\n",
       "600              1.399\n",
       "700              1.396\n",
       "800              1.392\n",
       "900              1.386\n",
       "1000             1.381\n",
       "1100             1.374\n",
       "1200             1.368\n",
       "1300             1.362\n",
       "1400             1.356\n",
       "1500             1.350\n",
       "1600             1.345\n",
       "1700             1.340\n",
       "1800             1.336\n",
       "1900             1.332\n",
       "2000             1.329\n",
       "2100             1.326\n",
       "2200             1.323\n",
       "2300             1.320\n",
       "2400             1.318\n",
       "2500             1.315\n",
       "2600             1.313\n",
       "2700             1.311\n",
       "2800             1.309\n",
       "2900             1.307\n",
       "3000             1.306\n",
       "3100             1.304\n",
       "3200             1.303\n",
       "3300             1.301\n",
       "3400             1.300\n",
       "3500             1.299"
      ]
     },
     "execution_count": 68,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "kTablaING"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 69,
   "id": "dabe5f19",
   "metadata": {
    "scrolled": true
   },
   "outputs": [
    {
     "data": {
      "text/html": [
       "<div>\n",
       "<style scoped>\n",
       "    .dataframe tbody tr th:only-of-type {\n",
       "        vertical-align: middle;\n",
       "    }\n",
       "\n",
       "    .dataframe tbody tr th {\n",
       "        vertical-align: top;\n",
       "    }\n",
       "\n",
       "    .dataframe thead th {\n",
       "        text-align: right;\n",
       "    }\n",
       "</style>\n",
       "<table border=\"1\" class=\"dataframe\">\n",
       "  <thead>\n",
       "    <tr style=\"text-align: right;\">\n",
       "      <th></th>\n",
       "      <th>Compuesto</th>\n",
       "      <th>Btu/mol</th>\n",
       "      <th>J/mol</th>\n",
       "      <th>Peso de la formula</th>\n",
       "      <th>Estado</th>\n",
       "      <th>Cp(kJ/kmol*K)</th>\n",
       "      <th>Cp(Btu/lbmol*R)</th>\n",
       "      <th>k</th>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>Formula</th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "    </tr>\n",
       "  </thead>\n",
       "  <tbody>\n",
       "    <tr>\n",
       "      <th>AR</th>\n",
       "      <td>Argón</td>\n",
       "      <td>0</td>\n",
       "      <td>0</td>\n",
       "      <td>39.9480</td>\n",
       "      <td>Gas</td>\n",
       "      <td>20.786</td>\n",
       "      <td>4.968</td>\n",
       "      <td>1.666</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>C</th>\n",
       "      <td>Carbono (grafito)</td>\n",
       "      <td>0</td>\n",
       "      <td>0</td>\n",
       "      <td>12.0112</td>\n",
       "      <td>Sólido</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>CO</th>\n",
       "      <td>Monóxido de carbono</td>\n",
       "      <td>-47517</td>\n",
       "      <td>-110525</td>\n",
       "      <td>28.0106</td>\n",
       "      <td>Gas</td>\n",
       "      <td>29.143</td>\n",
       "      <td>6.695</td>\n",
       "      <td>1.399</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>CO2</th>\n",
       "      <td>Bióxido de carbono</td>\n",
       "      <td>-169179</td>\n",
       "      <td>-393510</td>\n",
       "      <td>44.0100</td>\n",
       "      <td>Gas</td>\n",
       "      <td>37.128</td>\n",
       "      <td>8.874</td>\n",
       "      <td>1.288</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>CH4</th>\n",
       "      <td>Metano</td>\n",
       "      <td>-32162</td>\n",
       "      <td>-74809</td>\n",
       "      <td>16.0430</td>\n",
       "      <td>Gas</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>C2H6</th>\n",
       "      <td>Etano</td>\n",
       "      <td>-36408</td>\n",
       "      <td>-84685</td>\n",
       "      <td>32.0701</td>\n",
       "      <td>Gas</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>C3H8</th>\n",
       "      <td>Propano</td>\n",
       "      <td>-44647</td>\n",
       "      <td>-103849</td>\n",
       "      <td>44.0976</td>\n",
       "      <td>Gas</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>C4H10</th>\n",
       "      <td>n-butano</td>\n",
       "      <td>-63480</td>\n",
       "      <td>-147655</td>\n",
       "      <td>58.1248</td>\n",
       "      <td>Líquido</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>C7H16</th>\n",
       "      <td>n-heptano</td>\n",
       "      <td>-96471</td>\n",
       "      <td>-224392</td>\n",
       "      <td>100.2064</td>\n",
       "      <td>Líquido</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>C8H18</th>\n",
       "      <td>n-octano</td>\n",
       "      <td>-107462</td>\n",
       "      <td>-249957</td>\n",
       "      <td>114.2336</td>\n",
       "      <td>Líquido</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>H</th>\n",
       "      <td>Átomo de hidrógeno</td>\n",
       "      <td>93708</td>\n",
       "      <td>217965</td>\n",
       "      <td>1.0080</td>\n",
       "      <td>Gas</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>H2</th>\n",
       "      <td>Hidrógeno</td>\n",
       "      <td>0</td>\n",
       "      <td>0</td>\n",
       "      <td>2.0159</td>\n",
       "      <td>Gas</td>\n",
       "      <td>28.833</td>\n",
       "      <td>6.891</td>\n",
       "      <td>1.405</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>H2O</th>\n",
       "      <td>Agua</td>\n",
       "      <td>-103963</td>\n",
       "      <td>-241818</td>\n",
       "      <td>18.0153</td>\n",
       "      <td>Gas</td>\n",
       "      <td>33.577</td>\n",
       "      <td>8.025</td>\n",
       "      <td>1.329</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>HE</th>\n",
       "      <td>Helio</td>\n",
       "      <td>0</td>\n",
       "      <td>0</td>\n",
       "      <td>4.0026</td>\n",
       "      <td>Gas</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>N</th>\n",
       "      <td>Átomo de nitrógeno</td>\n",
       "      <td>203226</td>\n",
       "      <td>472704</td>\n",
       "      <td>14.0067</td>\n",
       "      <td>Gas</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>N2</th>\n",
       "      <td>Nitrógeno</td>\n",
       "      <td>0</td>\n",
       "      <td>0</td>\n",
       "      <td>28.0134</td>\n",
       "      <td>Gas</td>\n",
       "      <td>29.125</td>\n",
       "      <td>6.961</td>\n",
       "      <td>1.399</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>NO</th>\n",
       "      <td>Oxido nítrico</td>\n",
       "      <td>38800</td>\n",
       "      <td>90249</td>\n",
       "      <td>30.0061</td>\n",
       "      <td>Gas</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>NO2</th>\n",
       "      <td>Bióxido de nitrógeno</td>\n",
       "      <td>14264</td>\n",
       "      <td>33178</td>\n",
       "      <td>46.0055</td>\n",
       "      <td>Gas</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>NH3</th>\n",
       "      <td>Amoniaco</td>\n",
       "      <td>-19823</td>\n",
       "      <td>-46108</td>\n",
       "      <td>17.0306</td>\n",
       "      <td>Gas</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>O</th>\n",
       "      <td>Átomo de oxígeno</td>\n",
       "      <td>107124</td>\n",
       "      <td>249170</td>\n",
       "      <td>15.9994</td>\n",
       "      <td>Gas</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>O2</th>\n",
       "      <td>Oxígeno</td>\n",
       "      <td>0</td>\n",
       "      <td>0</td>\n",
       "      <td>31.9988</td>\n",
       "      <td>Gas</td>\n",
       "      <td>29.375</td>\n",
       "      <td>7.021</td>\n",
       "      <td>1.394</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>OH</th>\n",
       "      <td>Hidróxilo</td>\n",
       "      <td>16747</td>\n",
       "      <td>38954</td>\n",
       "      <td>17.0074</td>\n",
       "      <td>Gas</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>SO2</th>\n",
       "      <td>Bióxido de azufre</td>\n",
       "      <td>0</td>\n",
       "      <td>0</td>\n",
       "      <td>64.0628</td>\n",
       "      <td>Gas</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "      <td>NaN</td>\n",
       "    </tr>\n",
       "  </tbody>\n",
       "</table>\n",
       "</div>"
      ],
      "text/plain": [
       "                    Compuesto  Btu/mol   J/mol  Peso de la formula   Estado  \\\n",
       "Formula                                                                       \n",
       "AR                      Argón        0       0             39.9480      Gas   \n",
       "C           Carbono (grafito)        0       0             12.0112   Sólido   \n",
       "CO        Monóxido de carbono   -47517 -110525             28.0106      Gas   \n",
       "CO2        Bióxido de carbono  -169179 -393510             44.0100      Gas   \n",
       "CH4                    Metano   -32162  -74809             16.0430      Gas   \n",
       "C2H6                    Etano   -36408  -84685             32.0701      Gas   \n",
       "C3H8                  Propano   -44647 -103849             44.0976      Gas   \n",
       "C4H10                n-butano   -63480 -147655             58.1248  Líquido   \n",
       "C7H16               n-heptano   -96471 -224392            100.2064  Líquido   \n",
       "C8H18                n-octano  -107462 -249957            114.2336  Líquido   \n",
       "H          Átomo de hidrógeno    93708  217965              1.0080      Gas   \n",
       "H2                  Hidrógeno        0       0              2.0159      Gas   \n",
       "H2O                      Agua  -103963 -241818             18.0153      Gas   \n",
       "HE                      Helio        0       0              4.0026      Gas   \n",
       "N          Átomo de nitrógeno   203226  472704             14.0067      Gas   \n",
       "N2                  Nitrógeno        0       0             28.0134      Gas   \n",
       "NO              Oxido nítrico    38800   90249             30.0061      Gas   \n",
       "NO2      Bióxido de nitrógeno    14264   33178             46.0055      Gas   \n",
       "NH3                  Amoniaco   -19823  -46108             17.0306      Gas   \n",
       "O            Átomo de oxígeno   107124  249170             15.9994      Gas   \n",
       "O2                    Oxígeno        0       0             31.9988      Gas   \n",
       "OH                  Hidróxilo    16747   38954             17.0074      Gas   \n",
       "SO2         Bióxido de azufre        0       0             64.0628      Gas   \n",
       "\n",
       "         Cp(kJ/kmol*K)  Cp(Btu/lbmol*R)      k  \n",
       "Formula                                         \n",
       "AR              20.786            4.968  1.666  \n",
       "C                  NaN              NaN    NaN  \n",
       "CO              29.143            6.695  1.399  \n",
       "CO2             37.128            8.874  1.288  \n",
       "CH4                NaN              NaN    NaN  \n",
       "C2H6               NaN              NaN    NaN  \n",
       "C3H8               NaN              NaN    NaN  \n",
       "C4H10              NaN              NaN    NaN  \n",
       "C7H16              NaN              NaN    NaN  \n",
       "C8H18              NaN              NaN    NaN  \n",
       "H                  NaN              NaN    NaN  \n",
       "H2              28.833            6.891  1.405  \n",
       "H2O             33.577            8.025  1.329  \n",
       "HE                 NaN              NaN    NaN  \n",
       "N                  NaN              NaN    NaN  \n",
       "N2              29.125            6.961  1.399  \n",
       "NO                 NaN              NaN    NaN  \n",
       "NO2                NaN              NaN    NaN  \n",
       "NH3                NaN              NaN    NaN  \n",
       "O                  NaN              NaN    NaN  \n",
       "O2              29.375            7.021  1.394  \n",
       "OH                 NaN              NaN    NaN  \n",
       "SO2                NaN              NaN    NaN  "
      ]
     },
     "execution_count": 69,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "#Tabla de los compuestos para 25°C con índice en la formula\n",
    "compuestosTabla=CAL_FORM.set_index(\"Formula\") \n",
    "compuestosTabla"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 70,
   "id": "513d1152",
   "metadata": {
    "scrolled": true
   },
   "outputs": [],
   "source": [
    "#Tabla para el O2\n",
    "oxigenoTablaING=O2_ING.set_index(\"Temperatura (R)\")\n",
    "oxigenoTablaSI=O2_SI.set_index(\"Temperatura (K)\")\n",
    "dioxidoCarbonoTablaING=CO2_ING.set_index(\"Temperatura (R)\")\n",
    "dioxidoCarbonoTablaSI=CO2_SI.set_index(\"Temperatura (K)\")\n",
    "aguaTablaING=H2O_ING.set_index(\"Temperatura (R)\")\n",
    "aguaTablaSI=H2O_SI.set_index(\"Temperatura (K)\")"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 71,
   "id": "9afd7830",
   "metadata": {
    "scrolled": true
   },
   "outputs": [
    {
     "data": {
      "text/html": [
       "<div>\n",
       "<style scoped>\n",
       "    .dataframe tbody tr th:only-of-type {\n",
       "        vertical-align: middle;\n",
       "    }\n",
       "\n",
       "    .dataframe tbody tr th {\n",
       "        vertical-align: top;\n",
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       "</style>\n",
       "<table border=\"1\" class=\"dataframe\">\n",
       "  <thead>\n",
       "    <tr style=\"text-align: right;\">\n",
       "      <th></th>\n",
       "      <th>Cp (kJ/kmol*K)</th>\n",
       "      <th>h (kJ/kmol)</th>\n",
       "      <th>s (kJ/kmol*K)</th>\n",
       "      <th>g (kJ/kmol)</th>\n",
       "      <th>Pr</th>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>Temperatura (K)</th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "    </tr>\n",
       "  </thead>\n",
       "  <tbody>\n",
       "    <tr>\n",
       "      <th>298.15</th>\n",
       "      <td>33.577</td>\n",
       "      <td>-241816.1</td>\n",
       "      <td>188.713</td>\n",
       "      <td>-298080.8</td>\n",
       "      <td>0.7199</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>300.00</th>\n",
       "      <td>33.586</td>\n",
       "      <td>-241753.9</td>\n",
       "      <td>188.921</td>\n",
       "      <td>-298430.1</td>\n",
       "      <td>0.7382</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>350.00</th>\n",
       "      <td>33.884</td>\n",
       "      <td>-240067.5</td>\n",
       "      <td>194.119</td>\n",
       "      <td>-308009.2</td>\n",
       "      <td>1.3794</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>400.00</th>\n",
       "      <td>34.263</td>\n",
       "      <td>-238364.2</td>\n",
       "      <td>198.668</td>\n",
       "      <td>-317831.2</td>\n",
       "      <td>2.3840</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>450.00</th>\n",
       "      <td>34.706</td>\n",
       "      <td>-236640.2</td>\n",
       "      <td>202.728</td>\n",
       "      <td>-327867.9</td>\n",
       "      <td>3.8850</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>500.00</th>\n",
       "      <td>35.200</td>\n",
       "      <td>-234892.7</td>\n",
       "      <td>206.410</td>\n",
       "      <td>-338097.8</td>\n",
       "      <td>6.0490</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>550.00</th>\n",
       "      <td>35.734</td>\n",
       "      <td>-233119.5</td>\n",
       "      <td>209.790</td>\n",
       "      <td>-348503.9</td>\n",
       "      <td>9.0830</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>600.00</th>\n",
       "      <td>36.297</td>\n",
       "      <td>-231318.8</td>\n",
       "      <td>212.923</td>\n",
       "      <td>-359072.6</td>\n",
       "      <td>13.2400</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>650.00</th>\n",
       "      <td>36.881</td>\n",
       "      <td>-229489.4</td>\n",
       "      <td>215.851</td>\n",
       "      <td>-369792.8</td>\n",
       "      <td>18.8300</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>700.00</th>\n",
       "      <td>37.480</td>\n",
       "      <td>-227630.5</td>\n",
       "      <td>218.606</td>\n",
       "      <td>-380654.8</td>\n",
       "      <td>26.2280</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>750.00</th>\n",
       "      <td>38.089</td>\n",
       "      <td>-225741.3</td>\n",
       "      <td>221.213</td>\n",
       "      <td>-391650.9</td>\n",
       "      <td>35.8850</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>800.00</th>\n",
       "      <td>38.705</td>\n",
       "      <td>-223821.5</td>\n",
       "      <td>223.691</td>\n",
       "      <td>-402774.0</td>\n",
       "      <td>48.3450</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>850.00</th>\n",
       "      <td>39.327</td>\n",
       "      <td>-221870.7</td>\n",
       "      <td>226.056</td>\n",
       "      <td>-414018.1</td>\n",
       "      <td>64.2500</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>900.00</th>\n",
       "      <td>39.956</td>\n",
       "      <td>-219888.6</td>\n",
       "      <td>228.321</td>\n",
       "      <td>-425378.0</td>\n",
       "      <td>84.3800</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>950.00</th>\n",
       "      <td>40.594</td>\n",
       "      <td>-217874.9</td>\n",
       "      <td>230.499</td>\n",
       "      <td>-436848.8</td>\n",
       "      <td>109.6400</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1000.00</th>\n",
       "      <td>41.245</td>\n",
       "      <td>-215829.0</td>\n",
       "      <td>232.597</td>\n",
       "      <td>-448426.5</td>\n",
       "      <td>141.1200</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1050.00</th>\n",
       "      <td>41.921</td>\n",
       "      <td>-213749.8</td>\n",
       "      <td>234.626</td>\n",
       "      <td>-460107.4</td>\n",
       "      <td>180.1200</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1100.00</th>\n",
       "      <td>42.576</td>\n",
       "      <td>-211637.3</td>\n",
       "      <td>236.592</td>\n",
       "      <td>-471888.1</td>\n",
       "      <td>228.1000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1150.00</th>\n",
       "      <td>43.209</td>\n",
       "      <td>-209492.6</td>\n",
       "      <td>238.498</td>\n",
       "      <td>-483765.5</td>\n",
       "      <td>287.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1200.00</th>\n",
       "      <td>43.822</td>\n",
       "      <td>-207316.8</td>\n",
       "      <td>240.350</td>\n",
       "      <td>-495737.0</td>\n",
       "      <td>358.5000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1250.00</th>\n",
       "      <td>44.415</td>\n",
       "      <td>-205110.8</td>\n",
       "      <td>242.151</td>\n",
       "      <td>-507799.8</td>\n",
       "      <td>445.3000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1300.00</th>\n",
       "      <td>44.988</td>\n",
       "      <td>-202875.6</td>\n",
       "      <td>243.904</td>\n",
       "      <td>-519951.3</td>\n",
       "      <td>549.8000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1350.00</th>\n",
       "      <td>45.542</td>\n",
       "      <td>-200612.3</td>\n",
       "      <td>245.613</td>\n",
       "      <td>-532189.4</td>\n",
       "      <td>675.2000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1400.00</th>\n",
       "      <td>46.078</td>\n",
       "      <td>-198321.7</td>\n",
       "      <td>247.279</td>\n",
       "      <td>-544511.9</td>\n",
       "      <td>825.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1450.00</th>\n",
       "      <td>46.596</td>\n",
       "      <td>-196004.8</td>\n",
       "      <td>248.905</td>\n",
       "      <td>-556916.6</td>\n",
       "      <td>1003.2000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1500.00</th>\n",
       "      <td>47.096</td>\n",
       "      <td>-193662.4</td>\n",
       "      <td>250.493</td>\n",
       "      <td>-569401.8</td>\n",
       "      <td>1214.3000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1550.00</th>\n",
       "      <td>47.580</td>\n",
       "      <td>191295.4</td>\n",
       "      <td>252.045</td>\n",
       "      <td>-581965.3</td>\n",
       "      <td>1463.6000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1600.00</th>\n",
       "      <td>48.047</td>\n",
       "      <td>-188904.7</td>\n",
       "      <td>253.563</td>\n",
       "      <td>-594605.6</td>\n",
       "      <td>1756.8000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1650.00</th>\n",
       "      <td>48.498</td>\n",
       "      <td>-186491.0</td>\n",
       "      <td>255.049</td>\n",
       "      <td>-607321.1</td>\n",
       "      <td>2100.4000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1700.00</th>\n",
       "      <td>48.934</td>\n",
       "      <td>-184055.1</td>\n",
       "      <td>256.503</td>\n",
       "      <td>-620109.9</td>\n",
       "      <td>2501.9000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1750.00</th>\n",
       "      <td>49.335</td>\n",
       "      <td>-181597.8</td>\n",
       "      <td>257.927</td>\n",
       "      <td>-632970.9</td>\n",
       "      <td>2969.5000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1800.00</th>\n",
       "      <td>49.762</td>\n",
       "      <td>-179119.8</td>\n",
       "      <td>259.324</td>\n",
       "      <td>-645902.3</td>\n",
       "      <td>3512.4000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1850.00</th>\n",
       "      <td>50.154</td>\n",
       "      <td>-176621.9</td>\n",
       "      <td>260.692</td>\n",
       "      <td>-658902.8</td>\n",
       "      <td>4141.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1900.00</th>\n",
       "      <td>50.533</td>\n",
       "      <td>-174104.6</td>\n",
       "      <td>262.035</td>\n",
       "      <td>-671971.0</td>\n",
       "      <td>4867.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1950.00</th>\n",
       "      <td>50.898</td>\n",
       "      <td>-171568.8</td>\n",
       "      <td>263.352</td>\n",
       "      <td>-685105.8</td>\n",
       "      <td>5702.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2000.00</th>\n",
       "      <td>51.251</td>\n",
       "      <td>-169015.0</td>\n",
       "      <td>264.645</td>\n",
       "      <td>-698305.9</td>\n",
       "      <td>6662.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2050.00</th>\n",
       "      <td>51.592</td>\n",
       "      <td>-166443.9</td>\n",
       "      <td>265.915</td>\n",
       "      <td>-711570.0</td>\n",
       "      <td>7761.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2100.00</th>\n",
       "      <td>51.921</td>\n",
       "      <td>-163856.0</td>\n",
       "      <td>267.162</td>\n",
       "      <td>-724896.9</td>\n",
       "      <td>9017.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2150.00</th>\n",
       "      <td>52.239</td>\n",
       "      <td>-161252.0</td>\n",
       "      <td>268.388</td>\n",
       "      <td>-738285.9</td>\n",
       "      <td>10449.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2200.00</th>\n",
       "      <td>52.545</td>\n",
       "      <td>-158632.3</td>\n",
       "      <td>269.592</td>\n",
       "      <td>-751735.4</td>\n",
       "      <td>12078.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2250.00</th>\n",
       "      <td>52.841</td>\n",
       "      <td>-155997.6</td>\n",
       "      <td>270.776</td>\n",
       "      <td>-765244.7</td>\n",
       "      <td>13927.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2300.00</th>\n",
       "      <td>53.127</td>\n",
       "      <td>-153348.4</td>\n",
       "      <td>271.941</td>\n",
       "      <td>-778812.8</td>\n",
       "      <td>16020.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2350.00</th>\n",
       "      <td>53.402</td>\n",
       "      <td>-150685.1</td>\n",
       "      <td>273.087</td>\n",
       "      <td>-792438.6</td>\n",
       "      <td>18387.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2400.00</th>\n",
       "      <td>53.669</td>\n",
       "      <td>-148008.3</td>\n",
       "      <td>274.214</td>\n",
       "      <td>-806121.1</td>\n",
       "      <td>21056.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2450.00</th>\n",
       "      <td>53.926</td>\n",
       "      <td>-145318.4</td>\n",
       "      <td>275.323</td>\n",
       "      <td>-819859.7</td>\n",
       "      <td>24062.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2500.00</th>\n",
       "      <td>54.175</td>\n",
       "      <td>-142615.8</td>\n",
       "      <td>276.415</td>\n",
       "      <td>-833653.2</td>\n",
       "      <td>27439.0000</td>\n",
       "    </tr>\n",
       "  </tbody>\n",
       "</table>\n",
       "</div>"
      ],
      "text/plain": [
       "                 Cp (kJ/kmol*K)  h (kJ/kmol)  s (kJ/kmol*K)  g (kJ/kmol)  \\\n",
       "Temperatura (K)                                                            \n",
       "298.15                   33.577    -241816.1        188.713    -298080.8   \n",
       "300.00                   33.586    -241753.9        188.921    -298430.1   \n",
       "350.00                   33.884    -240067.5        194.119    -308009.2   \n",
       "400.00                   34.263    -238364.2        198.668    -317831.2   \n",
       "450.00                   34.706    -236640.2        202.728    -327867.9   \n",
       "500.00                   35.200    -234892.7        206.410    -338097.8   \n",
       "550.00                   35.734    -233119.5        209.790    -348503.9   \n",
       "600.00                   36.297    -231318.8        212.923    -359072.6   \n",
       "650.00                   36.881    -229489.4        215.851    -369792.8   \n",
       "700.00                   37.480    -227630.5        218.606    -380654.8   \n",
       "750.00                   38.089    -225741.3        221.213    -391650.9   \n",
       "800.00                   38.705    -223821.5        223.691    -402774.0   \n",
       "850.00                   39.327    -221870.7        226.056    -414018.1   \n",
       "900.00                   39.956    -219888.6        228.321    -425378.0   \n",
       "950.00                   40.594    -217874.9        230.499    -436848.8   \n",
       "1000.00                  41.245    -215829.0        232.597    -448426.5   \n",
       "1050.00                  41.921    -213749.8        234.626    -460107.4   \n",
       "1100.00                  42.576    -211637.3        236.592    -471888.1   \n",
       "1150.00                  43.209    -209492.6        238.498    -483765.5   \n",
       "1200.00                  43.822    -207316.8        240.350    -495737.0   \n",
       "1250.00                  44.415    -205110.8        242.151    -507799.8   \n",
       "1300.00                  44.988    -202875.6        243.904    -519951.3   \n",
       "1350.00                  45.542    -200612.3        245.613    -532189.4   \n",
       "1400.00                  46.078    -198321.7        247.279    -544511.9   \n",
       "1450.00                  46.596    -196004.8        248.905    -556916.6   \n",
       "1500.00                  47.096    -193662.4        250.493    -569401.8   \n",
       "1550.00                  47.580     191295.4        252.045    -581965.3   \n",
       "1600.00                  48.047    -188904.7        253.563    -594605.6   \n",
       "1650.00                  48.498    -186491.0        255.049    -607321.1   \n",
       "1700.00                  48.934    -184055.1        256.503    -620109.9   \n",
       "1750.00                  49.335    -181597.8        257.927    -632970.9   \n",
       "1800.00                  49.762    -179119.8        259.324    -645902.3   \n",
       "1850.00                  50.154    -176621.9        260.692    -658902.8   \n",
       "1900.00                  50.533    -174104.6        262.035    -671971.0   \n",
       "1950.00                  50.898    -171568.8        263.352    -685105.8   \n",
       "2000.00                  51.251    -169015.0        264.645    -698305.9   \n",
       "2050.00                  51.592    -166443.9        265.915    -711570.0   \n",
       "2100.00                  51.921    -163856.0        267.162    -724896.9   \n",
       "2150.00                  52.239    -161252.0        268.388    -738285.9   \n",
       "2200.00                  52.545    -158632.3        269.592    -751735.4   \n",
       "2250.00                  52.841    -155997.6        270.776    -765244.7   \n",
       "2300.00                  53.127    -153348.4        271.941    -778812.8   \n",
       "2350.00                  53.402    -150685.1        273.087    -792438.6   \n",
       "2400.00                  53.669    -148008.3        274.214    -806121.1   \n",
       "2450.00                  53.926    -145318.4        275.323    -819859.7   \n",
       "2500.00                  54.175    -142615.8        276.415    -833653.2   \n",
       "\n",
       "                         Pr  \n",
       "Temperatura (K)              \n",
       "298.15               0.7199  \n",
       "300.00               0.7382  \n",
       "350.00               1.3794  \n",
       "400.00               2.3840  \n",
       "450.00               3.8850  \n",
       "500.00               6.0490  \n",
       "550.00               9.0830  \n",
       "600.00              13.2400  \n",
       "650.00              18.8300  \n",
       "700.00              26.2280  \n",
       "750.00              35.8850  \n",
       "800.00              48.3450  \n",
       "850.00              64.2500  \n",
       "900.00              84.3800  \n",
       "950.00             109.6400  \n",
       "1000.00            141.1200  \n",
       "1050.00            180.1200  \n",
       "1100.00            228.1000  \n",
       "1150.00            287.0000  \n",
       "1200.00            358.5000  \n",
       "1250.00            445.3000  \n",
       "1300.00            549.8000  \n",
       "1350.00            675.2000  \n",
       "1400.00            825.0000  \n",
       "1450.00           1003.2000  \n",
       "1500.00           1214.3000  \n",
       "1550.00           1463.6000  \n",
       "1600.00           1756.8000  \n",
       "1650.00           2100.4000  \n",
       "1700.00           2501.9000  \n",
       "1750.00           2969.5000  \n",
       "1800.00           3512.4000  \n",
       "1850.00           4141.0000  \n",
       "1900.00           4867.0000  \n",
       "1950.00           5702.0000  \n",
       "2000.00           6662.0000  \n",
       "2050.00           7761.0000  \n",
       "2100.00           9017.0000  \n",
       "2150.00          10449.0000  \n",
       "2200.00          12078.0000  \n",
       "2250.00          13927.0000  \n",
       "2300.00          16020.0000  \n",
       "2350.00          18387.0000  \n",
       "2400.00          21056.0000  \n",
       "2450.00          24062.0000  \n",
       "2500.00          27439.0000  "
      ]
     },
     "execution_count": 71,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "aguaTablaSI"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 72,
   "id": "6d0098d7",
   "metadata": {
    "scrolled": true
   },
   "outputs": [
    {
     "data": {
      "text/html": [
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       "<table border=\"1\" class=\"dataframe\">\n",
       "  <thead>\n",
       "    <tr style=\"text-align: right;\">\n",
       "      <th></th>\n",
       "      <th>Cp (kJ/kmol*K)</th>\n",
       "      <th>h (kJ/kmol)</th>\n",
       "      <th>s (kJ/kmol*K)</th>\n",
       "      <th>g (kJ/kmol)</th>\n",
       "      <th>Pr</th>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>Temperatura (K)</th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "      <th></th>\n",
       "    </tr>\n",
       "  </thead>\n",
       "  <tbody>\n",
       "    <tr>\n",
       "      <th>298.15</th>\n",
       "      <td>33.577</td>\n",
       "      <td>-241816.1</td>\n",
       "      <td>188.713</td>\n",
       "      <td>-298080.8</td>\n",
       "      <td>0.7199</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>300.00</th>\n",
       "      <td>33.586</td>\n",
       "      <td>-241753.9</td>\n",
       "      <td>188.921</td>\n",
       "      <td>-298430.1</td>\n",
       "      <td>0.7382</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>350.00</th>\n",
       "      <td>33.884</td>\n",
       "      <td>-240067.5</td>\n",
       "      <td>194.119</td>\n",
       "      <td>-308009.2</td>\n",
       "      <td>1.3794</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>400.00</th>\n",
       "      <td>34.263</td>\n",
       "      <td>-238364.2</td>\n",
       "      <td>198.668</td>\n",
       "      <td>-317831.2</td>\n",
       "      <td>2.3840</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>450.00</th>\n",
       "      <td>34.706</td>\n",
       "      <td>-236640.2</td>\n",
       "      <td>202.728</td>\n",
       "      <td>-327867.9</td>\n",
       "      <td>3.8850</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>500.00</th>\n",
       "      <td>35.200</td>\n",
       "      <td>-234892.7</td>\n",
       "      <td>206.410</td>\n",
       "      <td>-338097.8</td>\n",
       "      <td>6.0490</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>550.00</th>\n",
       "      <td>35.734</td>\n",
       "      <td>-233119.5</td>\n",
       "      <td>209.790</td>\n",
       "      <td>-348503.9</td>\n",
       "      <td>9.0830</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>600.00</th>\n",
       "      <td>36.297</td>\n",
       "      <td>-231318.8</td>\n",
       "      <td>212.923</td>\n",
       "      <td>-359072.6</td>\n",
       "      <td>13.2400</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>650.00</th>\n",
       "      <td>36.881</td>\n",
       "      <td>-229489.4</td>\n",
       "      <td>215.851</td>\n",
       "      <td>-369792.8</td>\n",
       "      <td>18.8300</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>700.00</th>\n",
       "      <td>37.480</td>\n",
       "      <td>-227630.5</td>\n",
       "      <td>218.606</td>\n",
       "      <td>-380654.8</td>\n",
       "      <td>26.2280</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>750.00</th>\n",
       "      <td>38.089</td>\n",
       "      <td>-225741.3</td>\n",
       "      <td>221.213</td>\n",
       "      <td>-391650.9</td>\n",
       "      <td>35.8850</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>800.00</th>\n",
       "      <td>38.705</td>\n",
       "      <td>-223821.5</td>\n",
       "      <td>223.691</td>\n",
       "      <td>-402774.0</td>\n",
       "      <td>48.3450</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>850.00</th>\n",
       "      <td>39.327</td>\n",
       "      <td>-221870.7</td>\n",
       "      <td>226.056</td>\n",
       "      <td>-414018.1</td>\n",
       "      <td>64.2500</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>900.00</th>\n",
       "      <td>39.956</td>\n",
       "      <td>-219888.6</td>\n",
       "      <td>228.321</td>\n",
       "      <td>-425378.0</td>\n",
       "      <td>84.3800</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>950.00</th>\n",
       "      <td>40.594</td>\n",
       "      <td>-217874.9</td>\n",
       "      <td>230.499</td>\n",
       "      <td>-436848.8</td>\n",
       "      <td>109.6400</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1000.00</th>\n",
       "      <td>41.245</td>\n",
       "      <td>-215829.0</td>\n",
       "      <td>232.597</td>\n",
       "      <td>-448426.5</td>\n",
       "      <td>141.1200</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1050.00</th>\n",
       "      <td>41.921</td>\n",
       "      <td>-213749.8</td>\n",
       "      <td>234.626</td>\n",
       "      <td>-460107.4</td>\n",
       "      <td>180.1200</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1100.00</th>\n",
       "      <td>42.576</td>\n",
       "      <td>-211637.3</td>\n",
       "      <td>236.592</td>\n",
       "      <td>-471888.1</td>\n",
       "      <td>228.1000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1150.00</th>\n",
       "      <td>43.209</td>\n",
       "      <td>-209492.6</td>\n",
       "      <td>238.498</td>\n",
       "      <td>-483765.5</td>\n",
       "      <td>287.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1200.00</th>\n",
       "      <td>43.822</td>\n",
       "      <td>-207316.8</td>\n",
       "      <td>240.350</td>\n",
       "      <td>-495737.0</td>\n",
       "      <td>358.5000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1250.00</th>\n",
       "      <td>44.415</td>\n",
       "      <td>-205110.8</td>\n",
       "      <td>242.151</td>\n",
       "      <td>-507799.8</td>\n",
       "      <td>445.3000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1300.00</th>\n",
       "      <td>44.988</td>\n",
       "      <td>-202875.6</td>\n",
       "      <td>243.904</td>\n",
       "      <td>-519951.3</td>\n",
       "      <td>549.8000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1350.00</th>\n",
       "      <td>45.542</td>\n",
       "      <td>-200612.3</td>\n",
       "      <td>245.613</td>\n",
       "      <td>-532189.4</td>\n",
       "      <td>675.2000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1400.00</th>\n",
       "      <td>46.078</td>\n",
       "      <td>-198321.7</td>\n",
       "      <td>247.279</td>\n",
       "      <td>-544511.9</td>\n",
       "      <td>825.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1450.00</th>\n",
       "      <td>46.596</td>\n",
       "      <td>-196004.8</td>\n",
       "      <td>248.905</td>\n",
       "      <td>-556916.6</td>\n",
       "      <td>1003.2000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1500.00</th>\n",
       "      <td>47.096</td>\n",
       "      <td>-193662.4</td>\n",
       "      <td>250.493</td>\n",
       "      <td>-569401.8</td>\n",
       "      <td>1214.3000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1550.00</th>\n",
       "      <td>47.580</td>\n",
       "      <td>191295.4</td>\n",
       "      <td>252.045</td>\n",
       "      <td>-581965.3</td>\n",
       "      <td>1463.6000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1600.00</th>\n",
       "      <td>48.047</td>\n",
       "      <td>-188904.7</td>\n",
       "      <td>253.563</td>\n",
       "      <td>-594605.6</td>\n",
       "      <td>1756.8000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1650.00</th>\n",
       "      <td>48.498</td>\n",
       "      <td>-186491.0</td>\n",
       "      <td>255.049</td>\n",
       "      <td>-607321.1</td>\n",
       "      <td>2100.4000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1700.00</th>\n",
       "      <td>48.934</td>\n",
       "      <td>-184055.1</td>\n",
       "      <td>256.503</td>\n",
       "      <td>-620109.9</td>\n",
       "      <td>2501.9000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1750.00</th>\n",
       "      <td>49.335</td>\n",
       "      <td>-181597.8</td>\n",
       "      <td>257.927</td>\n",
       "      <td>-632970.9</td>\n",
       "      <td>2969.5000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1800.00</th>\n",
       "      <td>49.762</td>\n",
       "      <td>-179119.8</td>\n",
       "      <td>259.324</td>\n",
       "      <td>-645902.3</td>\n",
       "      <td>3512.4000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1850.00</th>\n",
       "      <td>50.154</td>\n",
       "      <td>-176621.9</td>\n",
       "      <td>260.692</td>\n",
       "      <td>-658902.8</td>\n",
       "      <td>4141.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1900.00</th>\n",
       "      <td>50.533</td>\n",
       "      <td>-174104.6</td>\n",
       "      <td>262.035</td>\n",
       "      <td>-671971.0</td>\n",
       "      <td>4867.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1950.00</th>\n",
       "      <td>50.898</td>\n",
       "      <td>-171568.8</td>\n",
       "      <td>263.352</td>\n",
       "      <td>-685105.8</td>\n",
       "      <td>5702.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2000.00</th>\n",
       "      <td>51.251</td>\n",
       "      <td>-169015.0</td>\n",
       "      <td>264.645</td>\n",
       "      <td>-698305.9</td>\n",
       "      <td>6662.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2050.00</th>\n",
       "      <td>51.592</td>\n",
       "      <td>-166443.9</td>\n",
       "      <td>265.915</td>\n",
       "      <td>-711570.0</td>\n",
       "      <td>7761.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2100.00</th>\n",
       "      <td>51.921</td>\n",
       "      <td>-163856.0</td>\n",
       "      <td>267.162</td>\n",
       "      <td>-724896.9</td>\n",
       "      <td>9017.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2150.00</th>\n",
       "      <td>52.239</td>\n",
       "      <td>-161252.0</td>\n",
       "      <td>268.388</td>\n",
       "      <td>-738285.9</td>\n",
       "      <td>10449.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2200.00</th>\n",
       "      <td>52.545</td>\n",
       "      <td>-158632.3</td>\n",
       "      <td>269.592</td>\n",
       "      <td>-751735.4</td>\n",
       "      <td>12078.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2250.00</th>\n",
       "      <td>52.841</td>\n",
       "      <td>-155997.6</td>\n",
       "      <td>270.776</td>\n",
       "      <td>-765244.7</td>\n",
       "      <td>13927.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2300.00</th>\n",
       "      <td>53.127</td>\n",
       "      <td>-153348.4</td>\n",
       "      <td>271.941</td>\n",
       "      <td>-778812.8</td>\n",
       "      <td>16020.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2350.00</th>\n",
       "      <td>53.402</td>\n",
       "      <td>-150685.1</td>\n",
       "      <td>273.087</td>\n",
       "      <td>-792438.6</td>\n",
       "      <td>18387.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2400.00</th>\n",
       "      <td>53.669</td>\n",
       "      <td>-148008.3</td>\n",
       "      <td>274.214</td>\n",
       "      <td>-806121.1</td>\n",
       "      <td>21056.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2450.00</th>\n",
       "      <td>53.926</td>\n",
       "      <td>-145318.4</td>\n",
       "      <td>275.323</td>\n",
       "      <td>-819859.7</td>\n",
       "      <td>24062.0000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2500.00</th>\n",
       "      <td>54.175</td>\n",
       "      <td>-142615.8</td>\n",
       "      <td>276.415</td>\n",
       "      <td>-833653.2</td>\n",
       "      <td>27439.0000</td>\n",
       "    </tr>\n",
       "  </tbody>\n",
       "</table>\n",
       "</div>"
      ],
      "text/plain": [
       "                 Cp (kJ/kmol*K)  h (kJ/kmol)  s (kJ/kmol*K)  g (kJ/kmol)  \\\n",
       "Temperatura (K)                                                            \n",
       "298.15                   33.577    -241816.1        188.713    -298080.8   \n",
       "300.00                   33.586    -241753.9        188.921    -298430.1   \n",
       "350.00                   33.884    -240067.5        194.119    -308009.2   \n",
       "400.00                   34.263    -238364.2        198.668    -317831.2   \n",
       "450.00                   34.706    -236640.2        202.728    -327867.9   \n",
       "500.00                   35.200    -234892.7        206.410    -338097.8   \n",
       "550.00                   35.734    -233119.5        209.790    -348503.9   \n",
       "600.00                   36.297    -231318.8        212.923    -359072.6   \n",
       "650.00                   36.881    -229489.4        215.851    -369792.8   \n",
       "700.00                   37.480    -227630.5        218.606    -380654.8   \n",
       "750.00                   38.089    -225741.3        221.213    -391650.9   \n",
       "800.00                   38.705    -223821.5        223.691    -402774.0   \n",
       "850.00                   39.327    -221870.7        226.056    -414018.1   \n",
       "900.00                   39.956    -219888.6        228.321    -425378.0   \n",
       "950.00                   40.594    -217874.9        230.499    -436848.8   \n",
       "1000.00                  41.245    -215829.0        232.597    -448426.5   \n",
       "1050.00                  41.921    -213749.8        234.626    -460107.4   \n",
       "1100.00                  42.576    -211637.3        236.592    -471888.1   \n",
       "1150.00                  43.209    -209492.6        238.498    -483765.5   \n",
       "1200.00                  43.822    -207316.8        240.350    -495737.0   \n",
       "1250.00                  44.415    -205110.8        242.151    -507799.8   \n",
       "1300.00                  44.988    -202875.6        243.904    -519951.3   \n",
       "1350.00                  45.542    -200612.3        245.613    -532189.4   \n",
       "1400.00                  46.078    -198321.7        247.279    -544511.9   \n",
       "1450.00                  46.596    -196004.8        248.905    -556916.6   \n",
       "1500.00                  47.096    -193662.4        250.493    -569401.8   \n",
       "1550.00                  47.580     191295.4        252.045    -581965.3   \n",
       "1600.00                  48.047    -188904.7        253.563    -594605.6   \n",
       "1650.00                  48.498    -186491.0        255.049    -607321.1   \n",
       "1700.00                  48.934    -184055.1        256.503    -620109.9   \n",
       "1750.00                  49.335    -181597.8        257.927    -632970.9   \n",
       "1800.00                  49.762    -179119.8        259.324    -645902.3   \n",
       "1850.00                  50.154    -176621.9        260.692    -658902.8   \n",
       "1900.00                  50.533    -174104.6        262.035    -671971.0   \n",
       "1950.00                  50.898    -171568.8        263.352    -685105.8   \n",
       "2000.00                  51.251    -169015.0        264.645    -698305.9   \n",
       "2050.00                  51.592    -166443.9        265.915    -711570.0   \n",
       "2100.00                  51.921    -163856.0        267.162    -724896.9   \n",
       "2150.00                  52.239    -161252.0        268.388    -738285.9   \n",
       "2200.00                  52.545    -158632.3        269.592    -751735.4   \n",
       "2250.00                  52.841    -155997.6        270.776    -765244.7   \n",
       "2300.00                  53.127    -153348.4        271.941    -778812.8   \n",
       "2350.00                  53.402    -150685.1        273.087    -792438.6   \n",
       "2400.00                  53.669    -148008.3        274.214    -806121.1   \n",
       "2450.00                  53.926    -145318.4        275.323    -819859.7   \n",
       "2500.00                  54.175    -142615.8        276.415    -833653.2   \n",
       "\n",
       "                         Pr  \n",
       "Temperatura (K)              \n",
       "298.15               0.7199  \n",
       "300.00               0.7382  \n",
       "350.00               1.3794  \n",
       "400.00               2.3840  \n",
       "450.00               3.8850  \n",
       "500.00               6.0490  \n",
       "550.00               9.0830  \n",
       "600.00              13.2400  \n",
       "650.00              18.8300  \n",
       "700.00              26.2280  \n",
       "750.00              35.8850  \n",
       "800.00              48.3450  \n",
       "850.00              64.2500  \n",
       "900.00              84.3800  \n",
       "950.00             109.6400  \n",
       "1000.00            141.1200  \n",
       "1050.00            180.1200  \n",
       "1100.00            228.1000  \n",
       "1150.00            287.0000  \n",
       "1200.00            358.5000  \n",
       "1250.00            445.3000  \n",
       "1300.00            549.8000  \n",
       "1350.00            675.2000  \n",
       "1400.00            825.0000  \n",
       "1450.00           1003.2000  \n",
       "1500.00           1214.3000  \n",
       "1550.00           1463.6000  \n",
       "1600.00           1756.8000  \n",
       "1650.00           2100.4000  \n",
       "1700.00           2501.9000  \n",
       "1750.00           2969.5000  \n",
       "1800.00           3512.4000  \n",
       "1850.00           4141.0000  \n",
       "1900.00           4867.0000  \n",
       "1950.00           5702.0000  \n",
       "2000.00           6662.0000  \n",
       "2050.00           7761.0000  \n",
       "2100.00           9017.0000  \n",
       "2150.00          10449.0000  \n",
       "2200.00          12078.0000  \n",
       "2250.00          13927.0000  \n",
       "2300.00          16020.0000  \n",
       "2350.00          18387.0000  \n",
       "2400.00          21056.0000  \n",
       "2450.00          24062.0000  \n",
       "2500.00          27439.0000  "
      ]
     },
     "execution_count": 72,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "aguaTablaSI.loc[305]=np.NaN\n",
    "aguaTablaSI.sort_index()\n",
    "#aguaTablaSI.drop(305)\n",
    "#aguaTablaSI\n",
    "aguaTablaSI.interpolate(method='index',inplace=True)\n",
    "aguaTablaSI.sort_index()\n",
    "aguaTablaSI.drop(305,inplace=True)\n",
    "aguaTablaSI"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 73,
   "id": "805fdd16",
   "metadata": {},
   "outputs": [
    {
     "data": {
      "image/png": "iVBORw0KGgoAAAANSUhEUgAAAEYAAAAQCAYAAACr+QluAAAAOXRFWHRTb2Z0d2FyZQBNYXRwbG90bGliIHZlcnNpb24zLjcuMCwgaHR0cHM6Ly9tYXRwbG90bGliLm9yZy88F64QAAAACXBIWXMAABJ0AAASdAHeZh94AAAC1UlEQVR4nO3YT6hVVRQG8N+zF0lWBoI4KKykIiJCiEqCRAUJatKgSSQVFEiBVjoIQ9dbgdCgv1qRWNi/cTUqEOpBVEYQTYJIeSZNpMBKVOwP9Bqc/ey94933Ht+9Qz84LM7e+/u+ffdde92979j09LTzOBvj/TozcwPeLa+PRsSbrf4jWF6h/xIRyyq6V+BZ3IUlOIqPkBHx+6g4NXTRWtCHfCV24+QAn+PIHs/zFd0V+BYP4xu8hMPYjAOZuWQUnD6fq5NWz4zJzDHswzF8gK19vP6IiImuE8PrWIpNEbF7lueLeBI7sXEEnKH8axmzCWs1q3qqo+FAZOY1WI8jeK3VHcVrQ2YuGoYzCv+zFiYzb8BzeCUiPh9khosy84HM3JaZmzNzTWZeUBm7tsT9EfHvnFlFnMCXuBi3D8mpobPWnIXJzHG8h5+xrYMRLCucnXgZn+FQZq7uMfb6Eg9WtA6VeN2QnBo6a7UzZgdW4qGION3BaB/WaRZnEW7CHlyFTzLz5tb4xSUer+jNtF8+JKeGzlpnim9m3qrJkhci4kAHExGRrabvsTEzT2ILJnBvF62CsRLP5XA1H85ArQXM2UIHsX0EBm+UeGerfeYbWaw3LmuNmy+nhs5aMxlzif/36J+Z7UQAezNzr6YoPzFgAr+W2P6l+LHEWj24tsTZNWA+nBo6a83UmL/wVuX5roz5orx32WarSjzcap8scX1mtgv/pbgDp/H1kJwaOmuNQym0j/RSyswJTUF+Z/aVIDNvxNGI+K01fjleLa/vz+6LiKnM3K85SzyuOVmfoWoybE9EnBqGU063F2IqIv6Zj1bfu9IA3IenM3MSP+EEVuBuLMTHel8LHsNX2JWZ6/ADbsMazXZ4ZgScTzV3uKs1h7lz1qrelTpgEh8W8/vxFFZrttyDuCci/m6TImIKt+DtMqEtmgXdhVURcWwUnBq6ao2d/9uhN/4DhhVfnvoLXzUAAAAASUVORK5CYII=\n",
      "text/latex": [
       "$\\displaystyle 4500.0$"
      ],
      "text/plain": [
       "4500.0"
      ]
     },
     "execution_count": 73,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "aguaTablaING.index[-1]"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 74,
   "id": "768ce531",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Función para interpolar o no si es que existe una indice\n",
    "def interpolarTablas(tabla,indice):\n",
    "    \"\"\"Tabla se tiene que agregar el dataframe al cual se le agregará un valor\n",
    "    indice es el valor del indice\"\"\"\n",
    "    if indice in tabla.index:\n",
    "        return\n",
    "#     if indice <= tabla.index[0]: #Menor que el primero\n",
    "#         tabla.loc[indice]=np.NaN\n",
    "#         tabla.sort_index(inplace=True)\n",
    "#         tabla.interpolate(method=\"spline\",order = 1,inplace=True, limit_direction=\"both\", fill_value=\"extrapolate\")\n",
    "#     if indice >= tabla.index[-1]: #Mayor que el ultimo\n",
    "#         tabla.loc[indice]=np.NaN\n",
    "#         tabla.sort_index(inplace=True)\n",
    "#         tabla.interpolate(method=\"slinear\",order = 1,inplace=True, fill_value=\"extrapolate\", limit_direction=\"both\")\n",
    "        #         raise Exception(\"Escoger un indice(temperatura, altitud, etc) que no sea menor que el primer valor de indice ni mayor a este\")\n",
    "    if indice not in tabla.index: #Crear valor en el index\n",
    "        tabla.loc[indice]=np.NaN\n",
    "        tabla.sort_index(inplace=True)\n",
    "        tabla.interpolate(method=\"slinear\",inplace=True, limit_direction=\"both\")\n",
    "        tabla.interpolate(method=\"slinear\",inplace=True, fill_value=\"extrapolate\", limit_direction=\"both\")"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 191,
   "id": "f828bd67",
   "metadata": {},
   "outputs": [],
   "source": [
    "def interpolarTablasCuad(tabla, indice):\n",
    "    \"\"\"Tabla se tiene que agregar el dataframe al cual se le agregará un valor\n",
    "    índice es el valor del indice\n",
    "    Util para metodo cuadratico\"\"\"\n",
    "    if indice in tabla.index:\n",
    "        return\n",
    "    if indice <= tabla.index[0]: #Menor que el primero\n",
    "        tabla.loc[indice]=np.NaN\n",
    "        tabla.sort_index(inplace=True)\n",
    "        tabla.interpolate(method=\"cubic\",inplace=True, limit_direction=\"both\", fill_value=\"extrapolate\")\n",
    "    if indice not in tabla.index: #Crear valor en el index\n",
    "        tabla.loc[indice]=np.NaN\n",
    "        tabla.sort_index(inplace=True)\n",
    "        tabla.interpolate(method=\"quadratic\",inplace=True, limit_direction=\"both\")\n",
    "        tabla.interpolate(method=\"quadratic\",inplace=True, limit_direction=\"both\", fill_value=\"extrapolate\")"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 193,
   "id": "4c68d52d",
   "metadata": {},
   "outputs": [
    {
     "data": {
      "text/html": [
       "<div>\n",
       "<style scoped>\n",
       "    .dataframe tbody tr th:only-of-type {\n",
       "        vertical-align: middle;\n",
       "    }\n",
       "\n",
       "    .dataframe tbody tr th {\n",
       "        vertical-align: top;\n",
       "    }\n",
       "\n",
       "    .dataframe thead th {\n",
       "        text-align: right;\n",
       "    }\n",
       "</style>\n",
       "<table border=\"1\" class=\"dataframe\">\n",
       "  <thead>\n",
       "    <tr style=\"text-align: right;\">\n",
       "      <th></th>\n",
       "      <th>k(R)</th>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>Temperatura (R)</th>\n",
       "      <th></th>\n",
       "    </tr>\n",
       "  </thead>\n",
       "  <tbody>\n",
       "    <tr>\n",
       "      <th>100.0</th>\n",
       "      <td>1.411973</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>398.0</th>\n",
       "      <td>1.400014</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>400.0</th>\n",
       "      <td>1.400000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>500.0</th>\n",
       "      <td>1.400000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>600.0</th>\n",
       "      <td>1.399000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>700.0</th>\n",
       "      <td>1.396000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>800.0</th>\n",
       "      <td>1.392000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>900.0</th>\n",
       "      <td>1.386000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1000.0</th>\n",
       "      <td>1.381000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1100.0</th>\n",
       "      <td>1.374000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1200.0</th>\n",
       "      <td>1.368000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1300.0</th>\n",
       "      <td>1.362000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1400.0</th>\n",
       "      <td>1.356000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1500.0</th>\n",
       "      <td>1.350000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1600.0</th>\n",
       "      <td>1.345000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1700.0</th>\n",
       "      <td>1.340000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1800.0</th>\n",
       "      <td>1.336000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>1900.0</th>\n",
       "      <td>1.332000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2000.0</th>\n",
       "      <td>1.329000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2100.0</th>\n",
       "      <td>1.326000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2200.0</th>\n",
       "      <td>1.323000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2300.0</th>\n",
       "      <td>1.320000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2400.0</th>\n",
       "      <td>1.318000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2500.0</th>\n",
       "      <td>1.315000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2600.0</th>\n",
       "      <td>1.313000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2700.0</th>\n",
       "      <td>1.311000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2800.0</th>\n",
       "      <td>1.309000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>2900.0</th>\n",
       "      <td>1.307000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>3000.0</th>\n",
       "      <td>1.306000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>3100.0</th>\n",
       "      <td>1.304000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>3200.0</th>\n",
       "      <td>1.303000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>3300.0</th>\n",
       "      <td>1.301000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>3400.0</th>\n",
       "      <td>1.300000</td>\n",
       "    </tr>\n",
       "    <tr>\n",
       "      <th>3500.0</th>\n",
       "      <td>1.299000</td>\n",
       "    </tr>\n",
       "  </tbody>\n",
       "</table>\n",
       "</div>"
      ],
      "text/plain": [
       "                    k(R) \n",
       "Temperatura (R)          \n",
       "100.0            1.411973\n",
       "398.0            1.400014\n",
       "400.0            1.400000\n",
       "500.0            1.400000\n",
       "600.0            1.399000\n",
       "700.0            1.396000\n",
       "800.0            1.392000\n",
       "900.0            1.386000\n",
       "1000.0           1.381000\n",
       "1100.0           1.374000\n",
       "1200.0           1.368000\n",
       "1300.0           1.362000\n",
       "1400.0           1.356000\n",
       "1500.0           1.350000\n",
       "1600.0           1.345000\n",
       "1700.0           1.340000\n",
       "1800.0           1.336000\n",
       "1900.0           1.332000\n",
       "2000.0           1.329000\n",
       "2100.0           1.326000\n",
       "2200.0           1.323000\n",
       "2300.0           1.320000\n",
       "2400.0           1.318000\n",
       "2500.0           1.315000\n",
       "2600.0           1.313000\n",
       "2700.0           1.311000\n",
       "2800.0           1.309000\n",
       "2900.0           1.307000\n",
       "3000.0           1.306000\n",
       "3100.0           1.304000\n",
       "3200.0           1.303000\n",
       "3300.0           1.301000\n",
       "3400.0           1.300000\n",
       "3500.0           1.299000"
      ]
     },
     "execution_count": 193,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "# kTablaING.drop(100,inplace=True)\n",
    "# interpolarTablasCuad(kTablaING,398)\n",
    "# kTablaING"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 172,
   "id": "c3adc858",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Función para obtener la entalpia de alguna molecula mediante su temperatura\n",
    "def moleculaEntalpia(molecula,temperatura,u):\n",
    "    \"\"\"Ingresando el valor de la molecula, su temperatura y unidades \n",
    "    se puede conseguir su entalpia\n",
    "    molecula = 'butano','heptano','octano', 'O2', 'CO2', 'H2O', \"Aire seco\"\n",
    "    se pueden ingresar valores numericos para estas moleculas\n",
    "    molecula --> 'metano' = 1 = 'CH4'\n",
    "    molecula --> 'etano' = 2 = 'C2H6'\n",
    "    molecula --> 'propano' = 3 = 'C3H8'\n",
    "    molecula --> 'butano' = 4 = 'C4H10'\n",
    "    molecula --> 'heptano' = 7 = 'C7H16'\n",
    "    molecula --> 'octano' = 8 = 'C8H18'\n",
    "    molecula --> 'O2' \n",
    "    molecula --> 'CO2'\n",
    "    molecula --> 'H2O'\n",
    "    molecula --> 'Aire seco\n",
    "    \n",
    "    NOTA: Con alcanos siempre se usará la temperatura de 25°C=298K=537R aunque haya alguna ya puesta\n",
    "    'u' es para indicar la unidad que tendrá, si serán inglesas o sistema internacional (SI)\n",
    "    u = 0 = 'SI'  --> unidades SI. °K,J,mol*kg\n",
    "    u = 1 = 'ING' --> unidades ING. °R,Btu,mol*lb\n",
    "    \"\"\"\n",
    "    U=u\n",
    "    if type(molecula) is str:\n",
    "        molecula=molecula.upper()\n",
    "    if type(U) is str:\n",
    "        U=U.upper()\n",
    "    if U == 0 or U == \"SI\":\n",
    "        U=\"J/mol\"\n",
    "    if U == 1 or U == \"ING\":\n",
    "        U=\"Btu/mol\"\n",
    "    butano=1\n",
    "    heptano=2\n",
    "    octano=3\n",
    "    if (molecula == \"BUTANO\") or (molecula == 4) or (molecula == \"C4H10\"):\n",
    "        return compuestosTabla.loc[\"C4H10\",U]\n",
    "    if (molecula == \"HEPTANO\") or molecula == 7 or molecula == \"C7H16\":\n",
    "        return compuestosTabla.loc[\"C7H16\",U]\n",
    "    if molecula == (\"OCTANO\") or molecula == 8 or molecula == \"C8H18\":\n",
    "        return compuestosTabla.loc[\"C8H18\",U]\n",
    "    if molecula == \"METANO\" or molecula == 1 or molecula == \"CH4\" or molecula == \"C1H4\":\n",
    "        return compuestosTabla.loc[\"CH4\",U]\n",
    "    if molecula == 'ETANO' or molecula == 2 or molecula == \"C2H6\":\n",
    "        return compuestosTabla.loc[\"C2H6\",U]\n",
    "    if molecula == \"PROPANO\" or molecula == 3 or molecula == \"C3H8\":\n",
    "        return compuestosTabla.loc[\"C3H8\",U]\n",
    "    if u == 0 or U==\"SI\":\n",
    "        U=\"h (kJ/kmol)\"\n",
    "    if u == 1 or U ==\"ING\":\n",
    "        U=\"h (Btu/mol)\"\n",
    "    if molecula == (\"O2\") and U == \"h (kJ/kmol)\" :#SI\n",
    "        interpolarTablas(oxigenoTablaSI,temperatura)\n",
    "        return oxigenoTablaSI.loc[temperatura,U]\n",
    "    if molecula == (\"CO2\") and U == \"h (kJ/kmol)\":#SI\n",
    "        interpolarTablas(dioxidoCarbonoTablaSI,temperatura)\n",
    "        return  dioxidoCarbonoTablaSI.loc[temperatura,U]\n",
    "    if molecula == (\"H2O\") and U == \"h (kJ/kmol)\":#SI\n",
    "        interpolarTablas(aguaTablaSI,temperatura)\n",
    "        return aguaTablaSI.loc[temperatura,U]\n",
    "    if molecula == (\"AIRE SECO\") and U == \"h (kJ/kmol)\":#SI\n",
    "        interpolarTablas(aireSIt,temperatura)\n",
    "        return aireSIt.loc[temperatura,\"h(kJ/kmol)\"]\n",
    "    \n",
    "    if molecula == (\"O2\") and U == \"h (Btu/mol)\": #ING\n",
    "        interpolarTablas(oxigenoTablaING,temperatura)\n",
    "        return oxigenoTablaING.loc[temperatura,U]\n",
    "    if molecula == (\"CO2\") and U == \"h (Btu/mol)\": #ING\n",
    "        interpolarTablas(dioxidoCarbonoTablaING,temperatura)\n",
    "        return dioxidoCarbonoTablaING.loc[temperatura,U]\n",
    "    if molecula == (\"H2O\") and U == \"h (Btu/mol)\": #ING\n",
    "        interpolarTablas(aguaTablaING,temperatura)\n",
    "        return aguaTablaING.loc[temperatura,U]\n",
    "    if molecula == (\"AIRE SECO\") and U == \"h (Btu/mol)\":#ING\n",
    "        interpolarTablas(aireINGt,temperatura)\n",
    "        return aireINGt.loc[temperatura,\"h(Btu/mol)\"]\n",
    "    \n",
    "    raise Exception(\"Algo salió mal\")"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 78,
   "id": "5fb05e51",
   "metadata": {},
   "outputs": [
    {
     "data": {
      "image/png": "iVBORw0KGgoAAAANSUhEUgAAAEsAAAAQCAYAAABeB4LeAAAAOXRFWHRTb2Z0d2FyZQBNYXRwbG90bGliIHZlcnNpb24zLjcuMCwgaHR0cHM6Ly9tYXRwbG90bGliLm9yZy88F64QAAAACXBIWXMAABJ0AAASdAHeZh94AAACUUlEQVR4nO3XT+hOeRTH8ddPJhtWQ1mMJKVhIX9KVvKvJn8iihXFQnYYhBTHmcUYC/LDQpmJ/FkoYWGkmFEizRRLQiTyt9j4T/lZ3KseTx6/S7/n50nO5j7PPeee9+nc8/ne77eto6PDd6tmPZuZPDPnY2/5d1FE/NkgbhqWYhh+xD1cwJaION8q/B5fWkiFQgdgO552ErcJxzAKJ9COi5iJc5k5r1X4TZmszGzDbjzCYaxsENe/9D3A8Ih4WOObgH/xG/a3Ar9Zk7UEE7EQzz4RN7Cs4b/aQiEiTuMJ+rUKv8ublZlD8QfaI+JMJ+HX8BpjMrNvXZ5x6INTrcLvUhlmZk/swy2s7Sw+Ih5n5mpswaXMPKqQzmDMwEksbhV+V0/WeozEgoh4UeWBiNiK2YoXtwhrMAe3sadeHl+T/8FkZeZNhY6r2oGImFc+O0bxNjd/zuc+M1fhd2zDDtzHz9iIA5k5IiJWVcjTdH69DK/jZVUQ7pbA9+N/Fes+o9Dx2IQjEbG8xnUxM2eV+VZk5s6IuPGJPN3C/6BZETGpKqjOemNI+ftlZn4sZldm7lIsvMvKe9PL6+n64Ih4npn/Y5ZCWg2b1V38rlrgX+GvBr5RJewsrqBWIr3Ka6Ptwfv7r1uB39bss2FmbkD4yHEjM+fioGJTODoi7tT4puBvRSN+iohHNb7B+AHXI+JNd/GbejasYIcU+5jJuJyZRxQL7FCFRNqwprZRpf2j+BANws3u4jftbFjFIuItpuJXXFKsDyswFsfxS0S0twq/6TL8luwd7MFoMidYhl0AAAAASUVORK5CYII=\n",
      "text/latex": [
       "$\\displaystyle -48.48$"
      ],
      "text/plain": [
       "-48.480000000000004"
      ]
     },
     "execution_count": 78,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "moleculaEntalpia(\"aire seco\",537,1)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 79,
   "id": "3b75108d",
   "metadata": {},
   "outputs": [
    {
     "data": {
      "text/plain": [
       "-249957"
      ]
     },
     "execution_count": 79,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "moleculaEntalpia(molecula=\"C8H18\",temperatura=298.15,u=0) #SI"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 80,
   "id": "87494db1",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Ecuación de temperatura adiabatica de la llama a presión constante\n",
    "def ecTempAd():\n",
    "    Q,Hpr,Hre=sympy.symbols(\"Q H_pr H_re\",real=True)\n",
    "    eq=sympy.Eq(0,Hpr-Hre)\n",
    "    "
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 81,
   "id": "6e1d359b",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Función que regresa el valor de la temperatura después de iteraciones\n",
    "def temperaturaEntalpiaIteraciones(X,temperatura,entalpiaForm,u,tol,porcExcesoAire=0):\n",
    "    \"\"\"Mediante iteraciones se consigue una temperatura\n",
    "    \n",
    "    X --> Si X=8 se tendrá un octano de C8H18\n",
    "          Si X=1 se tendrá un metano de CH4 y demás \n",
    "          \n",
    "    temperatura --> Valor de temperatura, dependiente del argumento u\n",
    "    para sus unidades\n",
    "    \n",
    "    entalpiaForm --> el valor de la entalpia en la formación\n",
    "    \n",
    "    u --> Unidades\n",
    "    u = 0 -->(SI)\n",
    "    u = 1 -->(INGLES)\n",
    "    \n",
    "    tol --> Tolerancia\n",
    "    tol = 1e-9 \n",
    "    tol = 0.000001\n",
    "    \n",
    "    porcExcesoAire --> Porcentaje de exceso de aire\n",
    "    por defecto tiene un porcentaje de 0\n",
    "    si el porcentaje es de %150 entonces\n",
    "    porcExcesoAire=1.5\n",
    "    \"\"\"\n",
    "    \n",
    "    if u==0: #SI\n",
    "        a=300 #K\n",
    "        b=2500 #K\n",
    "    if u==1: #INGLES\n",
    "        a=600 #R\n",
    "        b=4500 #R\n",
    "    \n",
    "    t=0 #Valor medio\n",
    "    it=0 #N° de iteración\n",
    "    \n",
    "    if f(a)*f(b)>0:\n",
    "        raise Exception(\"Los valores no funcionaran para temperatura\")\n",
    "    while True:\n",
    "        t=(a+b)/2\n",
    "        if f(t)<0:\n",
    "            a=t\n",
    "        if f(t)>0:\n",
    "            b=t\n",
    "        \n",
    "        if np.abs(f(t)) < tol:\n",
    "            break\n",
    "        if it > 1000:\n",
    "            raise Exception(\"Se han hecho más de 1000 iteraciones y no se ha logrado conseguir el valor tolerado\")\n",
    "        it=it+1\n",
    "    return t\n",
    "    "
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 82,
   "id": "55665665",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Función para regresar el valor de la raíz de una función\n",
    "def raizFuncion(f,tol,u,a=None,b=None):\n",
    "    \"\"\"\"\"\"\n",
    "    it=0 #Iteración\n",
    "    if u==0 and (a is None) and (b is None): #SI\n",
    "        a=300 #K\n",
    "        b=2500 #K\n",
    "    if u==1 and (a is None) and (b is None): #INGLES\n",
    "        a=600 #R\n",
    "        b=4500 #R\n",
    "    t=0 #Raíz\n",
    "    \n",
    "    if f(a)*f(b) > 0:\n",
    "        raise Exception(\"La función se mantiene con el mismo signo en los extremos de la temperatura\")\n",
    "    while True:\n",
    "        t=(a+b)/2\n",
    "        if f(t)<0:\n",
    "            a=t\n",
    "        \n",
    "        if f(t)==0:\n",
    "            break\n",
    "        \n",
    "        if f(t)>0:\n",
    "            b=t\n",
    "        \n",
    "        if it == 1000:\n",
    "            raise Exception(\"Se han logrado las 1000 iteraciones y no se ha llegado al resultado\")\n",
    "        \n",
    "        if abs(f(t)) < tol:\n",
    "            print(f(t))\n",
    "            break\n",
    "        \n",
    "        it=it+1\n",
    "    print(\"N° de iteraciones: \"+str(it))\n",
    "    return t"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 83,
   "id": "6b82f52b",
   "metadata": {},
   "outputs": [],
   "source": [
    "#Función de relación combustible aire\n",
    "def relCombustibleAire(relCA=None,C=None,A=None,CM=None,AM=None):\n",
    "    \"\"\"La relación combustible-aire (f/a) se define como la masa de combustible sumi-\n",
    "    nistrada a un proceso de combustión, dividida entre la masa de aire suministrado a\n",
    "    un proceso de combustión, ambos sobre una base consistente, o en forma de ecuación\n",
    "    f'=f/a=combustible/aire=masa de combustible suministrado/masa de aire suministrado\n",
    "    f'=relCA=f/a=C/A\n",
    "    CM y AM son las masas/mol del combustible y aire respectivamente\n",
    "    \n",
    "    Con esta función se puede realizar un despeje del valor que no sea ingresado\n",
    "    Al menos deben haber 2 parametros ingresados en la función para su correcto\n",
    "    funcionamiento\n",
    "    Si no se ingresa ningún valor de parametro entonces sólo se imprimirá la ecuación\n",
    "    \"\"\"\n",
    "    relca, c, a, cm, am=sympy.symbols(\"f' f a cm am\",real=True)\n",
    "    eq=sympy.Eq(relca,c*cm/(a*am))\n",
    "    if relCA == None and C == None and A == None and CM ==None and AM == None:\n",
    "        return eq\n",
    "    eq=eq.subs(relca,relCA).subs(c,C).subs(a,A).subs(cm,CM).subs(am,AM)\n",
    "    val=sympy.solve(eq)[0]\n",
    "    return val"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 84,
   "id": "55d8a930",
   "metadata": {},
   "outputs": [],
   "source": [
    "def relCombustibleAireGases(relCA = None, C = None, CM = None, AM = None):\n",
    "    \"\"\"Lo mismo que relCombustibleAire, pero al agregar el gas ya se incluye su peso\n",
    "    molecular\n",
    "    CM --> masa ó moles del combustible\n",
    "    AM --> masa ó moles del aire\n",
    "    \n",
    "    C es el combustible, la lista es:\n",
    "    \"Metano\" -- \"CH4 --- 1\"\n",
    "    \"Etano\" --- \"C2H6 -- 2\"\n",
    "    \"Propano\" - \"C3H8 -- 3\"\n",
    "    \"Butano\" -- \"C4H10 - 4\"\n",
    "    \"Heptano\" - \"C7H16 - 7\"\n",
    "    \"Octano\" -- \"C8H18 - 8\"\n",
    "    Con esto se obtiene el peso molecular\n",
    "    \"\"\"\n",
    "    s = \"Peso de la formula\"\n",
    "    if type(C) is str:\n",
    "        C = C.upper()\n",
    "        \n",
    "    if C == \"METANO\" or C == \"CH4\" or C == 1:\n",
    "        c = compuestosTabla.loc[\"CH4\",s]\n",
    "    if C == \"ETANO\" or C == \"C2H6\" or C == 2:\n",
    "        c = compuestosTabla.loc[\"C2H6\",s]\n",
    "    if C == \"PROPANO\" or C == \"C3H8\" or C == 3:\n",
    "        c = compuestosTabla.loc[\"C3H8\",s]\n",
    "    if C == \"BUTANO\" or C == \"C4H10\" or C == 4:\n",
    "        c = compuestosTabla.loc[\"C4H10\",s]\n",
    "    if C == \"HEPTANO\" or C == \"C7H16\" or C == 7:\n",
    "        c = compuestosTabla.loc[\"C7H16\",s]\n",
    "    if C == \"OCTANO\" or C == \"C8H18\" or C == 8:\n",
    "        c = compuestosTabla.loc[\"C8H18\",s]\n",
    "    \n",
    "    return float(relCombustibleAire(relCA=relCA,C=c,A=aireSecoMol,CM=CM,AM=AM))"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 85,
   "id": "28601ef3",
   "metadata": {},
   "outputs": [],
   "source": [
    "def pesoCombustible(C):\n",
    "    \"\"\"C es el combustible, la lista es:\n",
    "    \"Metano\" -- \"CH4 --- 1\"\n",
    "    \"Etano\" --- \"C2H6 -- 2\"\n",
    "    \"Propano\" - \"C3H8 -- 3\"\n",
    "    \"Butano\" -- \"C4H10 - 4\"\n",
    "    \"Heptano\" - \"C7H16 - 7\"\n",
    "    \"Octano\" -- \"C8H18 - 8\"\n",
    "    Con esto se obtiene el peso molecular\"\"\"\n",
    "    s = \"Peso de la formula\"\n",
    "    if C == \"METANO\" or C == \"CH4\" or C == 1:\n",
    "        c = compuestosTabla.loc[\"CH4\",s]\n",
    "        return c\n",
    "    if C == \"ETANO\" or C == \"C2H6\" or C == 2:\n",
    "        c = compuestosTabla.loc[\"C2H6\",s]\n",
    "        return c\n",
    "    if C == \"PROPANO\" or C == \"C3H8\" or C == 3:\n",
    "        c = compuestosTabla.loc[\"C3H8\",s]\n",
    "        return c\n",
    "    if C == \"BUTANO\" or C == \"C4H10\" or C == 4:\n",
    "        c = compuestosTabla.loc[\"C4H10\",s]\n",
    "        return c\n",
    "    if C == \"HEPTANO\" or C == \"C7H16\" or C == 7:\n",
    "        c = compuestosTabla.loc[\"C7H16\",s]\n",
    "        return c\n",
    "    if C == \"OCTANO\" or C == \"C8H18\" or C == 8:\n",
    "        c = compuestosTabla.loc[\"C8H18\",s]\n",
    "        return c\n",
    "    \n",
    "    raise Exception(\"Ingresar un valor de C valido\")"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 86,
   "id": "6f0d0d03",
   "metadata": {},
   "outputs": [],
   "source": [
    "def porcAireTeorico(pAT=None,pEA=None):\n",
    "    \"\"\"El porcentaje teórico de aire es igual al porcentaje de exceso de aire + 100\n",
    "    %aire teórico= %exceso de aire+100\n",
    "    pAT=pEA+100\n",
    "    pAT --> %aire teórico\n",
    "    pEA --> %exceso de aire\"\"\"\n",
    "    pat, pea=sympy.symbols(\"%at %ea\")\n",
    "    eq=sympy.Eq(pat,pea+100)\n",
    "    eq=eq.subs(pat,pAT).subs(pea,pEA)\n",
    "    val=sympy.solve(eq)[0]\n",
    "    return val\n",
    "    "
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 87,
   "id": "c4af4b4a",
   "metadata": {},
   "outputs": [],
   "source": [
    "def tablaComposicionSalida(mCO2,mH2O,mAS,mO2):\n",
    "    \"\"\"Crea una tabla con los valores de salida\n",
    "    de la cámara de combustión para la composición\n",
    "    \n",
    "    Los parametros mCO2,mH2O,mAS,mO2 son los moles respectivos\n",
    "    \n",
    "    P.E tablaComposicionSalida(8,9,202.37,-12.5)\"\"\"\n",
    "    columnas=[\"ni\",\"Mi\",\"ni*Mi\"]\n",
    "    indice=[\"CO2\",\"H2O\",\"AS\", \"O2\"]\n",
    "    masas={\"Mi\":[44.01,18.02,28.97,32],\"ni\":[mCO2,mH2O,mAS,mO2]}\n",
    "    df=pd.DataFrame(index=indice, columns=columnas,data=masas)\n",
    "    df[\"ni*Mi\"]=df[\"ni\"]*df[\"Mi\"]\n",
    "    df.loc[\"Suma\"]=df.sum()\n",
    "    return df"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 88,
   "id": "aac3c4ef",
   "metadata": {},
   "outputs": [],
   "source": [
    "def tablaComposicionEntrada(xAlcano,mAS,mAlcano):\n",
    "    \"\"\"Crea una tabla con los valores de la entrada de la cámara\n",
    "    de combustión\n",
    "    \n",
    "    xAlcano --> El valor x del hidrocarburo alcano\n",
    "    mAS     --> mol de aire seco\n",
    "    mAlcano --> mol de alcano\n",
    "    PE. tablaComposicionEntrada(8,59.666,1)\"\"\"\n",
    "    X=xAlcano\n",
    "    Y=2*X+2\n",
    "    alcano=\"C{}H{}\".format(str(X),str(Y))\n",
    "    if X == 1:\n",
    "        pA=16.0430\n",
    "    if X == 2:\n",
    "        pA=32.0701\n",
    "    if X == 3:\n",
    "        pA=44.0976\n",
    "    if X == 4:\n",
    "        pA=58.1248\n",
    "    if X == 7:\n",
    "        pA=100.2064\n",
    "    if X == 8:\n",
    "        pA=114.2336\n",
    "    columnas=[\"ni\",\"Mi\",\"ni*Mi\"]\n",
    "    indice=[alcano,\"AS\"]\n",
    "    masas={\"Mi\":[pA,28.97],\"ni\":[mAlcano, mAS]}\n",
    "    df=pd.DataFrame(index=indice, columns=columnas, data=masas)\n",
    "    df[\"ni*Mi\"]=df[\"ni\"]*df[\"Mi\"]\n",
    "    df.loc[\"Suma\"]=df.sum()\n",
    "    return df"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "c4933bf9",
   "metadata": {},
   "source": [
    "# FIN DE COMBUSTIÓN -------------------------------------------------------------------------------"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "95b2b53e",
   "metadata": {},
   "source": [
    "# CICLO BÁSICO (MEDIO REAL)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 89,
   "id": "0bf4deba",
   "metadata": {},
   "outputs": [],
   "source": [
    "def moleculaEntropia (molecula,temperatura,u):\n",
    "    \"\"\"Ingresando el valor de la molecula, su temperatura y unidades \n",
    "    se puede conseguir su entropia\n",
    "    molecula = 'O2', 'CO2', 'H2O', \"Aire seco\"\n",
    "    se pueden ingresar valores numericos para estas moleculas\n",
    "    molecula --> 'O2' \n",
    "    molecula --> 'CO2' \n",
    "    molecula --> 'H2O' \n",
    "    molecula --> 'Aire seco'\n",
    "    u = 0 = 'SI'  --> unidades SI. °K,J,mol*kg\n",
    "    u = 1 = 'ING' --> unidades ING. °R,Btu,mol*lb\n",
    "    (NO USAR NUMEROS EN molecula NI u POR EL MOMENTO)\n",
    "    \"\"\"\n",
    "    entalpia=moleculaEntalpia(molecula,temperatura,u)\n",
    "    \n",
    "    if type(molecula) is str:\n",
    "        molecula=molecula.upper()\n",
    "    if type(u) is str:\n",
    "        u=u.upper()\n",
    "        \n",
    "    #Con la entalpia poder sacar la entropia\n",
    "    if u == 0 or u == \"SI\":\n",
    "        U=\"s (kJ/kmol*K)\"\n",
    "        H=\"h (kJ/kmol)\"\n",
    "        \n",
    "        if molecula == \"O2\" or molecula == 4:\n",
    "            return oxigenoTablaSI.reset_index().set_index(H).loc[entalpia, U]\n",
    "        if molecula == \"CO2\" or molecula == 5:\n",
    "            return dioxidoCarbonoTablaSI.reset_index().set_index(H).loc[entalpia, U]\n",
    "        if molecula == \"H2O\" or molecula == 6:\n",
    "            return aguaTablaSI.reset_index().set_index(H).loc[entalpia,U]\n",
    "        if molecula == \"AIRE SECO\" or molecula == 7:\n",
    "            return aireSIt.reset_index().set_index(\"h(kJ/kmol)\").loc[entalpia,\"s(kJ/kmol*K)\"]\n",
    "        \n",
    "    if u == 1 or u == \"ING\":\n",
    "        U=\"s (Btu/mol*R)\"\n",
    "        H=\"h (Btu/mol)\"\n",
    "        \n",
    "        if molecula == \"O2\" or molecula == 4:\n",
    "            return oxigenoTablaING.reset_index().set_index(H).loc[entalpia, U]\n",
    "        if molecula == \"CO2\" or molecula == 5:\n",
    "            return dioxidoCarbonoTablaING.reset_index().set_index(H).loc[entalpia, U]\n",
    "        if molecula == \"H2O\" or molecula == 6:\n",
    "            return aguaTablaING.reset_index().set_index(H).loc[entalpia,U]\n",
    "        if molecula == \"AIRE SECO\" or molecula == 7:\n",
    "            return aireINGt.reset_index().set_index(\"h(Btu/mol)\").loc[entalpia,\"s(Btu/mol*R)\"]\n",
    "        \n",
    "    raise Exception(\"No se cumplieron las condiciones de los parametros\")\n"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 90,
   "id": "9f2a5fed",
   "metadata": {},
   "outputs": [],
   "source": [
    "def ecuacionIsentropica(u, s3 = None, s4i = None,  p3 = None, p4 = None,molPr = None):\n",
    "    \"\"\"la expansión isentrópica en la turbina del generador del gas, permite despejar cualquier valor que no sea ingresado\n",
    "    Solamente un parametro debe mantenerse sin ingresar para que el despeje sea correcto\n",
    "    \n",
    "    Para base molar\n",
    "    0 = ~s4i-~s3-~R*ln(p4/p3)\n",
    "    \n",
    "    Con moles de productos\n",
    "    0 = S4i-S3-~R*npr*ln(p4/p3)\n",
    "    \n",
    "    \n",
    "    u = 0      --> SI\n",
    "    u = 1      --> ING\n",
    "    molPr = npr -> moles del producto\n",
    "    p3, p4 --> Presion 3 y 4 respectivamente\n",
    "    \n",
    "    S4i = ~s4i*n\n",
    "    S3 = ~s3*n\n",
    "    n [=] n° moles\n",
    "    \n",
    "    Con u = 0:\n",
    "    ~s4i, ~s3 [=] kJ/kmol*K\n",
    "    S4i, S3 [=] kJ/K\n",
    "    ~R = 8.31434 * 10^3 J/(mol*K)\n",
    "    \n",
    "    Con u = 1:\n",
    "    ~s4i, ~s3 [=] Btu/mol*R\n",
    "    S4i, S3 [=] Btu/R\n",
    "    ~R = 1.98718 Btu/(mol*R)\n",
    "    \n",
    "    s4i --> la entalpia 4 imaginaria de todos los productos\n",
    "    s3 ---> la entalpia 3 de todos los productos\n",
    "    p3 ---> la presión 3\n",
    "    p4 ---> la presión 4\n",
    "    molPr > moles de los productos de la reacción\n",
    "    u ----> unidades\n",
    "    \"\"\"\n",
    "    if u == 0: #SI\n",
    "        r=8.31434 #J/mol*K\n",
    "    if u == 1: #ING\n",
    "        r=1.98718 #Btu/mol*R\n",
    "    S4I,S3,R,N,P4,P3=sympy.symbols(\"S_4i S_3 R n_pr p4 p3\",real=True)\n",
    "    if molPr is not None:\n",
    "        \n",
    "        if (s3 is None) or (s4i is None):\n",
    "            \n",
    "            eq = sympy.Eq(S4I-S3-R*N*sympy.ln(P4/P3),0)\n",
    "            eq = eq.subs(S4I,s4i).subs(S3,s3).subs(R,r).subs(N,molPr).subs(P3,p3).subs(P4,p4)\n",
    "            return sympy.solve(eq)[0]\n",
    "        \n",
    "        if (p3 is None) or (p4 is None):\n",
    "            \n",
    "            eq = sympy.Eq(P4/P3,sympy.exp((S4I-S3)/(R*N)))\n",
    "            eq = eq.subs(S4I,s4i).subs(S3,s3).subs(R,r).subs(N,molPr).subs(P3,p3).subs(P4,p4)\n",
    "            return sympy.solve(eq)[0]\n",
    "            \n",
    "    raise Exception(\"Rellenar los parametros necesarios\")"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 91,
   "id": "e9b6459f",
   "metadata": {},
   "outputs": [],
   "source": [
    "def expansionIsentropica34i(u, s3 = None, s4i = None,  p3 = None, p4 = None,molPr = None):\n",
    "    \"\"\"la expansión isentrópica en la turbina del generador del gas, permite despejar cualquier valor que no sea ingresado\n",
    "    Solamente un parametro debe mantenerse sin ingresar para que el despeje sea correcto\n",
    "    \n",
    "    Para base molar\n",
    "    0 = ~s4i-~s3-~R*ln(p4/p3)\n",
    "    \n",
    "    Con moles de productos\n",
    "    0 = S4i-S3-~R*npr*ln(p4/p3)\n",
    "\n",
    "    \n",
    "    u = 0      --> SI\n",
    "    u = 1      --> ING\n",
    "    molPr = npr -> moles del producto\n",
    "    p3, p4 --> Presion 3 y 4 respectivamente\n",
    "    \n",
    "    S4i = ~s4i*n\n",
    "    S3 = ~s3*n\n",
    "    n [=] n° moles\n",
    "    \n",
    "    Con u = 0:\n",
    "    ~s4i, ~s3 [=] kJ/kmol*K\n",
    "    S4i, S3 [=] kJ/K\n",
    "    ~R = 8.31434 * 10^3 J/(mol*K)\n",
    "    \n",
    "    Con u = 1:\n",
    "    ~s4i, ~s3 [=] Btu/mol*R\n",
    "    S4i, S3 [=] Btu/R\n",
    "    ~R = 1.98718 Btu/(mol*R)\n",
    "    \n",
    "    s4i --> la entalpia 4 imaginaria de todos los productos\n",
    "    s3 ---> la entalpia 3 de todos los productos\n",
    "    p3 ---> la presión 3\n",
    "    p4 ---> la presión 4\n",
    "    molPr > moles de los productos de la reacción\n",
    "    u ----> unidades\n",
    "    \"\"\"\n",
    "    return ecuacionIsentropica(u=u,s3=s3,s4i=s4i,p3=p3,p4=p4,molPr=molPr)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 92,
   "id": "2230307f",
   "metadata": {},
   "outputs": [],
   "source": [
    "def expansionIsentropica45i(u, s4a = None, s5i = None,  p4 = None, p5 = None,molPr = None):\n",
    "    \"\"\"Más información en expansionIsentropica34i\n",
    "    \n",
    "    Con moles de productos\n",
    "    0 = S5i-S4r-~R*npr*ln(p5/p4)\n",
    "    \n",
    "    \"\"\"\n",
    "    return ecuacionIsentropica(u=u,s3=s4a,s4i=s5i,p3=p4,p4=p5,molPr=molPr)"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "e0354b9e",
   "metadata": {},
   "source": [
    "# FIN DE CICLO BÁSICO (MEDIO REAL)"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "fc0f29bc",
   "metadata": {},
   "source": [
    "# TURBINA DE GAS CON REGENERADOR"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 93,
   "id": "39b0fd38",
   "metadata": {},
   "outputs": [],
   "source": [
    "def eficienciaRegenerador(eficienciaReg, H2A=None, H5A=None, H25=None):\n",
    "    \"\"\"Se usa la formula\n",
    "    nreg=(h2.5-h2a)/(h5a-h2a)\n",
    "    El valor que no sea ingresado en los parametros será el despejado de la formula\n",
    "    \"\"\"\n",
    "    h25,h2a,h5a,nr = sympy.symbols(\"h_25 h_2a h_5a n_reg\",real=True)\n",
    "    eq=sympy.Eq(nr,(h25-h2a)/(h5a-h2a))\n",
    "    eq=eq.subs(h25,H25).subs(h2a,H2A).subs(h5a,H5A).subs(nr,eficienciaReg)\n",
    "    return sympy.solve(eq)[0]"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 94,
   "id": "5db9642d",
   "metadata": {},
   "outputs": [],
   "source": [
    "def formulasRegenerador():\n",
    "    h25,h2a,h5a,nr,qent,h3 = sympy.symbols(\"h_25 h_2a h_5a n_reg q_ent h_3\",real=True)\n",
    "    LEC,f,conv,conv2,wn, nt, ent=sympy.symbols(\"LEC f' 2545 28.965 w_neto n_t Delta_Hcomb\",real=True)\n",
    "    eq=sympy.Eq(nr,(h25-h2a)/(h5a-h2a))\n",
    "    eq2=sympy.Eq(qent,h3-h25)\n",
    "    eq3=sympy.Eq(LEC,conv/(nt*ent))\n",
    "    \n",
    "    return list([eq,eq2,eq3])"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 95,
   "id": "3347d298",
   "metadata": {},
   "outputs": [
    {
     "data": {
      "image/png": "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\n",
      "text/latex": [
       "$\\displaystyle \\left[ n_{reg} = \\frac{h_{25} - h_{2a}}{- h_{2a} + h_{5a}}, \\  q_{ent} = - h_{25} + h_{3}, \\  LEC = \\frac{2545}{\\Delta_{Hcomb} n_{t}}\\right]$"
      ],
      "text/plain": [
       "⎡        h₂₅ - h₂ₐ                              2545   ⎤\n",
       "⎢n_reg = ──────────, qₑₙₜ = -h₂₅ + h₃, LEC = ──────────⎥\n",
       "⎣        -h₂ₐ + h₅ₐ                          Δ_Hcomb⋅nₜ⎦"
      ]
     },
     "execution_count": 95,
     "metadata": {},
     "output_type": "execute_result"
    }
   ],
   "source": [
    "formulasRegenerador()"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "f121ef87",
   "metadata": {},
   "source": [
    "# FIN DE TURBINA DE GAS CON REGENERADOR"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "326eb59d",
   "metadata": {},
   "source": [
    "# Mecanica de fluidos"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 96,
   "id": "9d91d42c",
   "metadata": {
    "scrolled": true
   },
   "outputs": [],
   "source": [
    "# compuestosTabla"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 97,
   "id": "7af78180",
   "metadata": {},
   "outputs": [],
   "source": [
    "def valoresCompuestos(c,u):\n",
    "    \"\"\"\n",
    "    c -> Compuesto\n",
    "    c --> \"Ar\"\n",
    "    c --> \"CO\"\n",
    "    c --> \"CO2\"\n",
    "    c --> \"H2\"\n",
    "    c --> \"H2O\"\n",
    "    c --> \"N2\"\n",
    "    c --> \"O2\"\n",
    "    \n",
    "    u -> Unidades\n",
    "    u --> 0 --> SI \n",
    "    u --> 1 --> ING\n",
    "    Este regresa 5 valores en total\n",
    "    Peso molar, Cp[mol], Cp[lb/kg], k\n",
    "    \"\"\"\n",
    "    if type(c) is not str:\n",
    "       raise Exception(\"Ingresa un valor de compuesto correcto\")\n",
    "    c = c.upper()\n",
    "    \n",
    "    if u == 0:\n",
    "        cptext = \"Cp(kJ/kmol*K)\"\n",
    "    if u == 1:\n",
    "        cptext = \"Cp(Btu/lbmol*R)\"\n",
    "    \n",
    "    M = compuestosTabla.loc[c,\"Peso de la formula\"]\n",
    "    Cpmol=compuestosTabla.loc[c,cptext]\n",
    "    Cp = Cpmol/M\n",
    "    k = compuestosTabla.loc[c,\"k\"]\n",
    "    \n",
    "    return M, Cpmol, Cp, k"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 98,
   "id": "962b09a3",
   "metadata": {},
   "outputs": [],
   "source": [
    "def verificarEstancado(pd,pahogamiento,tent,k, p1, cp,u):\n",
    "    \"\"\"\n",
    "    pd -> Presión de descarga (presión después de garganta)\n",
    "    pahogamiento -> Presión de estancamiento\n",
    "    tent -> Temperatura de entrada\n",
    "    k -> Valor k\n",
    "    u -> Unidades\n",
    "    u --> 0 -> SI\n",
    "    u --> 1 -> INGLES\n",
    "    p1 -> Presión de entrada\n",
    "    cp -> Cp[kg/lb] NO USAR MOLAR\n",
    "    \"\"\"\n",
    "    if u == 0:\n",
    "        gc = 1\n",
    "        R = 8.31e3 #J/(molkg*K)\n",
    "    if u == 1:\n",
    "        gc = 32.174\n",
    "        R = 35.133\n",
    "        \n",
    "    if pd <= pahogamiento:\n",
    "        print(\"Estancado\\nLos valores entregados son\")\n",
    "        print(\"Pth, Tth, Vth\")\n",
    "        \n",
    "        pth = pahogamiento\n",
    "        tth = tent*(2/(k+1))\n",
    "        vth = float(sympy.sqrt(k*gc*R*tth))\n",
    "        return pth,tth,vth\n",
    "    \n",
    "    if pd > pahogamiento:\n",
    "        print(\"No estancado\\nLos valores entregados son\")\n",
    "        print(\"Pth, Tth, Vth\")\n",
    "        \n",
    "        pth = pd\n",
    "        tth = tent*(pth/p1)**((k-1)/k)\n",
    "        vth = sympy.sqrt(2*cp*(tent-tth)*25037)\n",
    "        return pth,tth,vth\n",
    "    \n",
    "    raise Exception(\"Algo sucedió\")"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "de8b7271",
   "metadata": {},
   "source": [
    "# Mecanica de fluidos FIN"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "d6602a52",
   "metadata": {},
   "source": [
    "# TURBINAS DE GAS PARA LA PROPULSIÓN DE AVIONES"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 99,
   "id": "b4a3f1c2",
   "metadata": {},
   "outputs": [],
   "source": [
    "def ISApropiedades(u,a=None, t=None, p=None):\n",
    "    \"\"\"\n",
    "    u -> unidades\n",
    "    u --> 0 -> SI\n",
    "    u --> 1 -> ING\n",
    "    a -> altura\n",
    "    a --> (m)\n",
    "    a --> (ft)\n",
    "    t -> temperatura\n",
    "    t --> (K)\n",
    "    t --> (R)\n",
    "    p -> presión\n",
    "    p --> (kPa)\n",
    "    p --> (psi)\n",
    "    Una vez puestas las unidades, con ingresar un valor se conseguiran los otros 2\n",
    "    Si:\n",
    "    a tiene valor regresará temperatura y presión\n",
    "    t tiene valor regresará altura y presión\n",
    "    p tiene valor regresará altura y temperatura\n",
    "    \"\"\"\n",
    "    U=u\n",
    "    if U == 0:\n",
    "        u = altitudTablaSI\n",
    "        temperaturaStr = \"Temperatura (K)\"\n",
    "        presionStr = \"Presión (kpa)\"\n",
    "        altitudStr = \"Altitud(m)\"\n",
    "    if U == 1:\n",
    "        u = altitudTablaING\n",
    "        temperaturaStr = \"Temperatura (R)\"\n",
    "        presionStr = \"Presión (psi)\"\n",
    "        altitudStr = \"Altitud(ft)\"\n",
    "    \n",
    "    if a is not None:\n",
    "        interpolarTablas(u,a)\n",
    "        T=u.loc[a,temperaturaStr]\n",
    "        P=u.loc[a,presionStr]\n",
    "        return T,P\n",
    "    \n",
    "    if t is not None:\n",
    "        u = u.reset_index().set_index(temperaturaStr)\n",
    "        interpolarTablas(u,t)\n",
    "        A=u.loc[t,altitudStr]\n",
    "        P=u.loc[t,presionStr]\n",
    "        return A,P\n",
    "    \n",
    "    if p is not None:\n",
    "        u = u.reset_index().set_index(presionStr)\n",
    "        interpolarTablas(u,p)\n",
    "        A=u.loc[p,altitudStr]\n",
    "        T=u.loc[p,temperaturaStr]\n",
    "        return A,T"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 100,
   "id": "e2c1598a",
   "metadata": {},
   "outputs": [],
   "source": [
    "def valorK (u,T):\n",
    "    \"\"\"\n",
    "    u --> Unidades\n",
    "    u -> 0 -> SI\n",
    "    u -> 1 -> ING\n",
    "    \n",
    "    T --> Temperatura\n",
    "    T -> °R -> ING\n",
    "    T -> °K -> SI\"\"\"\n",
    "    if u == 0:\n",
    "        interpolarTablasCuad(kTablaSI,T)\n",
    "        return kTablaSI.loc[T,\"k(K)\"]\n",
    "    if u == 1:\n",
    "        interpolarTablasCuad(kTablaING,T)\n",
    "        return kTablaING.loc[T,\"k(R) \"]\n",
    "    \n",
    "    raise Exception(\"Ten congruencia en los valores u y T\")"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 101,
   "id": "b10e59bf",
   "metadata": {},
   "outputs": [],
   "source": [
    "def valoresTablaAire(U,t=None,pr=None,s=None,h=None):\n",
    "    \"\"\"Con su respectivo valor se puede conseguir todo lo demás\n",
    "    Si tiene valor -> Entrega:\n",
    "    t  -> H,PR,S\n",
    "    pr -> H,T,S\n",
    "    s  -> H,T,PR\n",
    "    h  -> T,PR,S\n",
    "    \n",
    "    U -> Unidades\n",
    "    U --> 0 -> SI\n",
    "    U --> 1 -> ING\n",
    "    \n",
    "    Los valores entregados tienen unidad de masa -> kmol en SI, mol en ING\n",
    "    \"\"\"\n",
    "    if type(U) is not int:\n",
    "        raise Exception(\"Ingresa un valor correcto en las unidades\")\n",
    "    rd = 8\n",
    "    if U == 0: #SI\n",
    "        hs = \"h(kJ/kmol)\"\n",
    "        ts = \"Temperatura(K)\"\n",
    "        prs = \"Pr\"\n",
    "        ss = \"s(kJ/kmol*K)\"\n",
    "        if t is not None:\n",
    "            tabla = TemperaturaSI(t).loc[t]\n",
    "            H = round(tabla.loc[hs],rd)\n",
    "            S = round(tabla.loc[ss],rd)\n",
    "            PR = round(tabla.loc[prs],rd)\n",
    "            print(H,hs,\"|\",PR,prs,\"|\",S,ss)\n",
    "            return H,PR,S\n",
    "        if pr is not None:\n",
    "            tabla = PresionRelSI(pr).loc[pr]\n",
    "            T = round(tabla.loc[ts],rd)\n",
    "            H = round(tabla.loc[hs],rd)\n",
    "            S = round(tabla.loc[ss],rd)\n",
    "            print(H,hs,\"|\",T,ts,\"|\",S,ss)\n",
    "            return H,T,S\n",
    "        if s is not None:\n",
    "            tabla = EntropiaSI(s).loc[s]\n",
    "            H = round(tabla.loc[hs],rd)\n",
    "            T = round(tabla.loc[ts],rd)\n",
    "            PR = round(tabla.loc[prs],rd)\n",
    "            print(H,hs,\"|\",T,ts,\"|\",PR,prs)\n",
    "            return H,T,PR\n",
    "        if h is not None:\n",
    "            tabla = EntalpiaSI(h).loc[h]\n",
    "            T = round(tabla.loc[ts],rd)\n",
    "            PR = round(tabla.loc[prs],rd)\n",
    "            S = round(tabla.loc[ss],rd)\n",
    "            print(T,ts,\"|\",PR,prs,\"|\",S,ss)\n",
    "            return T,PR,S\n",
    "    if U == 1: #ING    \n",
    "        hs = \"h(Btu/mol)\"\n",
    "        ts = \"Temperatura(R)\"\n",
    "        prs = \"Pr\"\n",
    "        ss = \"s(Btu/mol*R)\"\n",
    "        if t is not None:\n",
    "            tabla = TemperaturaING(t).loc[t]\n",
    "            H = round(tabla.loc[hs],rd)\n",
    "            S = round(tabla.loc[ss],rd)\n",
    "            PR = round(tabla.loc[prs],rd)\n",
    "            print(H,hs,\"|\",PR,prs,\"|\",S,ss)\n",
    "            return H,PR,S\n",
    "        if pr is not None:\n",
    "            tabla = PresionRelING(pr).loc[pr]\n",
    "            T = round(tabla.loc[ts],rd)\n",
    "            H = round(tabla.loc[hs],rd)\n",
    "            S = round(tabla.loc[ss],rd)\n",
    "            print(H,hs,\"|\",T,ts,\"|\",S,ss)\n",
    "            return H,T,S\n",
    "        if s is not None:\n",
    "            tabla = EntropiaING(s).loc[s]\n",
    "            H = round(tabla.loc[hs],rd)\n",
    "            T = round(tabla.loc[ts],rd)\n",
    "            PR = round(tabla.loc[prs],rd)\n",
    "            print(H,hs,\"|\",T,ts,\"|\",PR,prs)\n",
    "            return H,T,PR\n",
    "        if h is not None:\n",
    "            tabla = EntalpiaING(h).loc[h]\n",
    "            T = round(tabla.loc[ts],rd)\n",
    "            PR = round(tabla.loc[prs],rd)\n",
    "            S = round(tabla.loc[ss],rd)\n",
    "            print(T,ts,\"|\",PR,prs,\"|\",S,ss)\n",
    "            return T,PR,S\n",
    "        \n",
    "    raise Exception(\"Algun parametro es incorrecto\")"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "4c00df72",
   "metadata": {},
   "source": [
    "# TURBINAS DE GAS PARA LA PROPULSIÓN DE AVIONES FIN"
   ]
  },
  {
   "cell_type": "markdown",
   "id": "67f69801",
   "metadata": {},
   "source": [
    "## PRUEBAS (IGNORAR)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 102,
   "id": "abee6744",
   "metadata": {},
   "outputs": [],
   "source": [
    "# aireSecoCombustion(8,18)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 103,
   "id": "89dfde3e",
   "metadata": {
    "scrolled": false
   },
   "outputs": [],
   "source": [
    "# aireSIt.loc[2630].rename_axis(\"Temperatura \")"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": null,
   "id": "2af4984b",
   "metadata": {},
   "outputs": [],
   "source": []
  },
  {
   "cell_type": "code",
   "execution_count": 104,
   "id": "b51bce0f",
   "metadata": {},
   "outputs": [],
   "source": [
    "# aireING.iloc[0]\n",
    "#Localizar mediante enteros del index"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 105,
   "id": "fed5f187",
   "metadata": {},
   "outputs": [],
   "source": [
    "# aireINGt.loc[4840]\n",
    "#Localizar en función de temperatura "
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 106,
   "id": "2342c9ee",
   "metadata": {},
   "outputs": [],
   "source": [
    "# TR in aireINGt.index()aireINGt.loc[4845]=[np.NaN,np.NaN,np.NaN,np.NaN]\n",
    "#Se crea una fila con la temperatura 4845 y no tiene valores a mostrar aún\n",
    "# aireINGt=aireINGt.sort_index()\n",
    "# #Hace que la posición de la temperatura esté ordenada\n",
    "# aireINGt.loc[4845]"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 107,
   "id": "767fc14c",
   "metadata": {},
   "outputs": [],
   "source": [
    "# aireINGt"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 108,
   "id": "91bec926",
   "metadata": {},
   "outputs": [],
   "source": [
    "# aireINGt.interpolate(method='index')\n"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 109,
   "id": "07fda3ca",
   "metadata": {},
   "outputs": [],
   "source": [
    "# aireINGt.loc[4885]=[np.NaN,np.NaN,np.NaN,np.NaN]\n",
    "# aireINGt"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 110,
   "id": "7324177f",
   "metadata": {},
   "outputs": [],
   "source": [
    "# aireINGt.interpolate(method='index')\n"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 111,
   "id": "a76230b9",
   "metadata": {},
   "outputs": [],
   "source": [
    "# 4847 not in aireINGt.index\n",
    "# #Condicional de encontrar valor de temperatura en el index"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 112,
   "id": "153f9656",
   "metadata": {
    "scrolled": true
   },
   "outputs": [],
   "source": [
    "# IndexCercanos(4820,aireINGt)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 113,
   "id": "ebd13e43",
   "metadata": {},
   "outputs": [],
   "source": [
    "# #FUNCIÓN VIEJA, NO USAR\n",
    "# #Definir función que me ayude a encontrar valores termodinámicos en función de su temperatura en Kelvin\n",
    "# def TemperaturaSI (TK):\n",
    "#     \"\"\"Docstring\n",
    "#     Definir función que me ayude a encontrar valores termodinámicos en función de su temperatura en Kelvin\n",
    "#     TemperaturaSI(TK)\n",
    "#     TK = Temperatura en Kelvin\"\"\"\n",
    "#     global aireSIt\n",
    "#     if TK not in aireSIt.index:\n",
    "#         aireSIt.loc[TK]=[np.NaN,np.NaN,np.NaN,np.NaN]\n",
    "#         aireSIt=aireSIt.sort_index()\n",
    "#         aireSIt=aireSIt.interpolate(method='index')\n",
    "#     return aireSIt.loc[TK].rename_axis('Temperatura(K)'+'       '+str(TK))"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 114,
   "id": "f0708116",
   "metadata": {},
   "outputs": [],
   "source": [
    "# #FUNCIÓN VIEJA, NO USAR\n",
    "# #Definir función que me ayude a encontrar valores termodinamicos en función de su temperatura en rankine\n",
    "# def TemperaturaING (TR):\n",
    "#     \"\"\"Docstring\n",
    "#     Definir función que me ayude a encontrar valores termodinamicos en función de su temperatura en rankine\n",
    "#     TemperaturaING(TR)\n",
    "#     TR = Temperatura en Rankine\"\"\"\n",
    "#     global aireINGt  #La variable global aireINGt se declara dentro de la función\n",
    "#     indexes=IndexCercanos(TR,aireINGt) #Valor para localizar el indice anterior y posterior al valor de temperatura\n",
    "#     if TR not in aireINGt.index:  #Busca que el valor de temperatura no exista, si existe entonces se salta lo que lleva sangria\n",
    "#         aireINGt.loc[TR]=[np.NaN,np.NaN,np.NaN,np.NaN] #Se crea una fila con la temperatura TR sin valores\n",
    "#         aireINGt=aireINGt.sort_index() #Se ordena basandose en su temperatura\n",
    "#         aireINGt=aireINGt.interpolate(method='index') #Se interpola los valores NaN\n",
    "#     return aireINGt.iloc[indexes] #.rename_axis('Temperatura(R)'+'       '+str(TR)) #Regresa en pantalla los valores termodinamicos"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 115,
   "id": "be3f73fd",
   "metadata": {},
   "outputs": [],
   "source": [
    "# aireINGt=aireINGt.drop(3025)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 116,
   "id": "8050a6c0",
   "metadata": {
    "scrolled": true
   },
   "outputs": [],
   "source": [
    "# aireINGt.index.is_monotonic_increasing\n",
    "# aireINGt.style"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 117,
   "id": "2c08ad96",
   "metadata": {
    "scrolled": true
   },
   "outputs": [],
   "source": [
    "# aireINGt.loc[[2820,2840,2860]]"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 118,
   "id": "c07b21a9",
   "metadata": {
    "scrolled": true
   },
   "outputs": [],
   "source": [
    "# aireINGt.iloc[208:210]"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 119,
   "id": "1dd20e27",
   "metadata": {
    "scrolled": true
   },
   "outputs": [],
   "source": [
    "# aireINGt.index.get_loc(4240.5, method='backfill')"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 120,
   "id": "bd4da3cd",
   "metadata": {},
   "outputs": [],
   "source": [
    "# indexCercanos1=aireINGt.index.get_indexer([4240.5], method='ffill')\n",
    "# indexCercanos2=aireINGt.index.get_indexer([4240.5], method='bfill')\n",
    "# indexCercanos=np.append(indexCercanos1,[indexCercanos2,indexCercanos2+1]) #+1 porque cuando el nuevo valor de temperatura se agregue, obtendra el valor de indexCercanos2\n",
    "# #indexCercanos=np.append(indexCercanos,indexCercanos2)\n",
    "# indexCercanos\n",
    "# #aireINGt.iloc[indexCercanos]"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 121,
   "id": "8962561b",
   "metadata": {
    "scrolled": true
   },
   "outputs": [],
   "source": [
    "\n",
    "# aireING.rename(dictLb,axis=1,copy=False) #Renombrar columnas a masa igual a lb para sistema ingles\n",
    "# aireSI.rename(dictGr,axis=1,copy=False)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 122,
   "id": "47df7481",
   "metadata": {
    "scrolled": true
   },
   "outputs": [],
   "source": [
    "# aireING.set_axis(['Temperatura(R)','Cp(Btu/lb*R)','h(Btu/lb)','s(Btu/lb*R)','Pr'],axis=\"columns\")\n",
    "# tablasLb=np.array(['Temperatura(R)','Cp(Btu/lb*R)','h(Btu/lb)','s(Btu/lb*R)','Pr'])\n",
    "# tablasLb\n",
    "# aireING.columns\n",
    "# #aireING=aireING.set_axis(tablasLb,axis=\"columns\",copy=False)\n",
    "# #aireING\n",
    "# aireSI.columns\n",
    "# #Formas de asignar valores a columnas\n",
    "#     #aireSI['Temperatura(K)'] = 1\n",
    "#     #aireSI.loc[:,'Temperatura(K)']=1\n",
    "# #aireSI.loc[]\n",
    "# aireSI.iloc[:,1:4]\n"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 123,
   "id": "2564c845",
   "metadata": {},
   "outputs": [],
   "source": [
    "# c=20*u.BTU/u.mol/u.rankine\n",
    "# substancia=1*u.mol\n",
    "# substancia\n",
    "# substancia.to(\"g\",\"chem\",mw=28.9647*u(\"g/mol\"))\n",
    "\n",
    "\n",
    "# substancia*28.9467*u('g/mol')\n",
    "# c*1/aireSecoMolING\n",
    "# #aireSecoMolagnitude"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 124,
   "id": "f4e817c6",
   "metadata": {
    "scrolled": false
   },
   "outputs": [],
   "source": [
    "# aireINGLb=aireING.copy()\n",
    "# aireINGLb.columns"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 125,
   "id": "36a852d6",
   "metadata": {
    "scrolled": true
   },
   "outputs": [],
   "source": [
    "# T1,T2,R,P1,P2,K=sympy.symbols('T_1 T_2 r_p P_1 P_2 k',real=True)\n",
    "# eq1=sympy.Eq(P2/P1,(T2/T1)**(K/(K-1)))\n",
    "# eq2=sympy.Eq(R,(T2/T1)**(K/(K-1)))\n",
    "\n",
    "\n",
    "# eq1=eq1.subs(T1,519).subs(P1,1).subs(P2,15.88).subs(K,1.4)\n",
    "# eq1\n",
    "# k=sympy.solve(eq1,T2)[0]\n",
    "# k+1"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 126,
   "id": "96df78fc",
   "metadata": {},
   "outputs": [],
   "source": [
    "# relCombustibleAireGases(C = 7, CM = 1, AM = 183.203383950465)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 127,
   "id": "df907f6b",
   "metadata": {
    "scrolled": true
   },
   "outputs": [],
   "source": [
    "# ecuacionIsentropica(1,10944.3,10549.6,176.4,molPr=188)"
   ]
  },
  {
   "cell_type": "code",
   "execution_count": 128,
   "id": "ca4c5496",
   "metadata": {
    "scrolled": true
   },
   "outputs": [],
   "source": [
    "# compuestosTabla.loc[\"CH4\"]\n",
    "#compuestosTabla.loc[\"CH4\",\"Peso de la formula\"]"
   ]
  }
 ],
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