Fixex2

.devcontainer/devcontainer.json

@@ -36,7 +36,9 @@
                 "ms-python.pylint",
                 "ms-python.black-formatter",
                 "ms-python.flake8",
-                "ms-python.pylint"
+                "ms-python.pylint",
+                "GitHub.copilot",
+                "GitHub.copilot-chat"
             ]
         }
     },

examples/CO2deprezzurizing.py

@@ -1,5 +1,21 @@
 # -*- coding: utf-8 -*-
 """
+This script demonstrates the process of CO2 depressurization using the NeqSim library.
+
+The script performs the following steps:
+1. Creates a fluid object using the SRK equation of state.
+2. Adds 100 moles of CO2 to the fluid.
+3. Sets the initial temperature to -25°C and pressure to 18 bara.
+4. Enables multi-phase and solid-phase checks for CO2.
+5. Performs a temperature-pressure (TP) flash calculation.
+6. Calculates the bubble point temperature.
+7. Prints the fluid properties before depressurization.
+8. Initializes the fluid properties and calculates the enthalpy.
+9. Sets the pressure to 1 bara and performs a pressure-enthalpy (PH) flash calculation.
+10. Prints the fluid properties after depressurization.
+
+The script also includes commented-out lines for performing dew point and solid phase flash calculations.
+
 Created on Tue Jun 23 10:37:26 2020
 
 @author: ESOL

examples/CarnotCycle.py

@@ -1,5 +1,42 @@
 # -*- coding: utf-8 -*-
 """
+This script simulates a Carnot cycle using the neqsim library for thermodynamic calculations.
+
+The Carnot cycle consists of four main processes:
+1. Isothermal Expansion (1-2): Heat is transferred reversibly from a high-temperature reservoir at constant temperature.
+2. Isentropic Expansion (2-3): Reversible adiabatic expansion of the gas, resulting in work output.
+3. Isothermal Compression (3-4): Heat is transferred reversibly to a low-temperature reservoir at constant temperature.
+4. Adiabatic Reversible Compression (4-1): The gas is compressed adiabatically and reversibly.
+
+The script performs the following steps:
+1. Initializes a fluid at thermodynamic equilibrium with specified components and conditions.
+2. Simulates the isothermal expansion process and calculates the state properties.
+3. Simulates the isentropic expansion process and calculates the state properties.
+4. Simulates the isothermal compression process and calculates the state properties.
+5. Simulates the adiabatic reversible compression process and calculates the state properties.
+6. Calculates the Carnot efficiency based on the heat transferred during the cycle.
+7. Plots the pressure-volume (PV) and temperature-entropy (TS) diagrams for the Carnot cycle.
+
+Variables:
+- P1: Initial pressure in bara.
+- T_hot: High temperature in Celsius.
+- T_cold: Low temperature in Celsius.
+- fluid_1: Thermodynamic fluid object.
+- T1, T2, T3, T4, T5: Temperatures at different states in Celsius.
+- P2, P3, P4, P5: Pressures at different states in bara.
+- H1, H2, H3, H4, H5: Enthalpies at different states in kJ/kg.
+- U1, U2, U3, U4, U5: Internal energies at different states in kJ/kg.
+- S1, S2, S3, S4, S5: Entropies at different states in kJ/kgK.
+- V1, V2, V3, V4, V5: Volumes at different states in m3.
+- dS: Change in entropy between states 1 and 2 in kJ/kgK.
+- QH: Heat added during the isothermal expansion in kJ.
+- QC: Heat rejected during the isothermal compression in kJ.
+- efficiency: Calculated Carnot efficiency.
+- efficiency2: Theoretical Carnot efficiency.
+
+Plots:
+- Pressure vs. Volume (PV) diagram.
+- Temperature vs. Entropy (TS) diagram.
 Created on Thu Jan  2 15:49:07 2020
 
 @author: esol
@@ -19,7 +56,7 @@
 fluid_1.setTemperature(T_hot, "C")
 fluid_1.setPressure(P1, "bara")
 TPflash(fluid_1)
-fluid_1.display()
+printFrame(fluid_1)
 T1 = fluid_1.getTemperature("C")
 H1 = fluid_1.getEnthalpy("kJ/kg")
 U1 = fluid_1.getInternalEnergy("kJ/kg")
@@ -30,7 +67,7 @@
 # 1-2: Isothermal Expansion. Heat is transferred reversibly from high temperature reservoir at constant temperature TH (isothermal heat addition or absorption).
 V2 = V1 * 1.5
 TVflash(fluid_1, V2, "m3")
-fluid_1.display()
+printFrame(fluid_1)
 T2 = fluid_1.getTemperature("C")
 P2 = fluid_1.getPressure("bara")
 H2 = fluid_1.getEnthalpy("kJ/kg")
@@ -40,7 +77,7 @@
 # 2-3: Isentropic (reversible adiabatic) expansion of the gas (isentropic work output).
 fluid_1.setTemperature(T_cold, "C")
 TSflash(fluid_1, S2, "kJ/kgK")
-fluid_1.display()
+printFrame(fluid_1)
 
 T3 = fluid_1.getTemperature("C")
 P3 = fluid_1.getPressure()
@@ -59,7 +96,7 @@
 S4 = fluid_1.getEntropy("kJ/kgK")
 V4 = fluid_1.getVolume("m3")
 
-fluid_1.display()
+printFrame(fluid_1)
 # 4-1 Adiabatic reversible compression.
 
 VSflash(fluid_1, V1, S4, "m3", "kJ/kgK")
@@ -69,7 +106,7 @@
 U5 = fluid_1.getInternalEnergy("kJ/kg")
 S5 = fluid_1.getEntropy("kJ/kgK")
 V5 = fluid_1.getVolume("m3")
-fluid_1.display()
+printFrame(fluid_1)
 
 dS = S2 - S1
 QH = (T_hot + 273.15) * dS

examples/compressorCalc.py

@@ -2,6 +2,7 @@
 """
 Created on Thu Jun  4 10:52:50 2020
 
+
 @author: ESOL
 """
 import pandas as pd

examples/jupyter/readEclipseE300format.ipynb

@@ -18,7 +18,7 @@
   },
   {
    "cell_type": "code",
-   "execution_count": 3,
+   "execution_count": 1,
    "metadata": {},
    "outputs": [],
    "source": [
@@ -36,7 +36,7 @@
   },
   {
    "cell_type": "code",
-   "execution_count": 4,
+   "execution_count": 2,
    "metadata": {},
    "outputs": [],
    "source": [
@@ -47,7 +47,7 @@
   },
   {
    "cell_type": "code",
-   "execution_count": 5,
+   "execution_count": 3,
    "metadata": {},
    "outputs": [
     {
@@ -85,8 +85,8 @@
        "      <th>0</th>\n",
        "      <td></td>\n",
        "      <td>total</td>\n",
-       "      <td>gas</td>\n",
-       "      <td>oil</td>\n",
+       "      <td>GAS</td>\n",
+       "      <td>OIL</td>\n",
        "      <td></td>\n",
        "      <td></td>\n",
        "      <td></td>\n",
@@ -95,8 +95,8 @@
        "      <th>1</th>\n",
        "      <td>nitrogen</td>\n",
        "      <td>1.328E-3</td>\n",
-       "      <td>1.37375E-3</td>\n",
-       "      <td>2.27017E-6</td>\n",
+       "      <td>1.37208E-3</td>\n",
+       "      <td>2.10134E-6</td>\n",
        "      <td></td>\n",
        "      <td></td>\n",
        "      <td>[mole fraction]</td>\n",
@@ -105,8 +105,8 @@
        "      <th>2</th>\n",
        "      <td>CO2</td>\n",
        "      <td>3.25865E-2</td>\n",
-       "      <td>3.36916E-2</td>\n",
-       "      <td>5.65258E-4</td>\n",
+       "      <td>3.36515E-2</td>\n",
+       "      <td>5.53463E-4</td>\n",
        "      <td></td>\n",
        "      <td></td>\n",
        "      <td>[mole fraction]</td>\n",
@@ -115,8 +115,8 @@
        "      <th>3</th>\n",
        "      <td>methane</td>\n",
        "      <td>8.39723E-1</td>\n",
-       "      <td>8.68521E-1</td>\n",
-       "      <td>5.27666E-3</td>\n",
+       "      <td>8.67475E-1</td>\n",
+       "      <td>5.02947E-3</td>\n",
        "      <td></td>\n",
        "      <td></td>\n",
        "      <td>[mole fraction]</td>\n",
@@ -125,8 +125,8 @@
        "      <th>4</th>\n",
        "      <td>ethane</td>\n",
        "      <td>4.83544E-2</td>\n",
-       "      <td>4.99564E-2</td>\n",
-       "      <td>1.93729E-3</td>\n",
+       "      <td>4.98992E-2</td>\n",
+       "      <td>1.89264E-3</td>\n",
        "      <td></td>\n",
        "      <td></td>\n",
        "      <td>[mole fraction]</td>\n",
@@ -198,11 +198,11 @@
       ],
       "text/plain": [
        "           0           1           2           3 4  5                 6\n",
-       "0                  total         gas         oil                       \n",
-       "1   nitrogen    1.328E-3  1.37375E-3  2.27017E-6        [mole fraction]\n",
-       "2        CO2  3.25865E-2  3.36916E-2  5.65258E-4        [mole fraction]\n",
-       "3    methane  8.39723E-1  8.68521E-1  5.27666E-3        [mole fraction]\n",
-       "4     ethane  4.83544E-2  4.99564E-2  1.93729E-3        [mole fraction]\n",
+       "0                  total         GAS         OIL                       \n",
+       "1   nitrogen    1.328E-3  1.37208E-3  2.10134E-6        [mole fraction]\n",
+       "2        CO2  3.25865E-2  3.36515E-2  5.53463E-4        [mole fraction]\n",
+       "3    methane  8.39723E-1  8.67475E-1  5.02947E-3        [mole fraction]\n",
+       "4     ethane  4.83544E-2  4.98992E-2  1.89264E-3        [mole fraction]\n",
        "..       ...         ...         ...         ... .. ..              ...\n",
        "59    Stream                                                          -\n",
        "60                                                                     \n",
@@ -213,7 +213,7 @@
        "[64 rows x 7 columns]"
       ]
      },
-     "execution_count": 5,
+     "execution_count": 3,
      "metadata": {},
      "output_type": "execute_result"
     }
@@ -232,7 +232,7 @@
   },
   {
    "cell_type": "code",
-   "execution_count": 8,
+   "execution_count": 4,
    "metadata": {},
    "outputs": [],
    "source": [
@@ -241,7 +241,7 @@
   },
   {
    "cell_type": "code",
-   "execution_count": 9,
+   "execution_count": 5,
    "metadata": {},
    "outputs": [
     {
@@ -279,8 +279,8 @@
        "      <th>0</th>\n",
        "      <td></td>\n",
        "      <td>total</td>\n",
-       "      <td>gas</td>\n",
-       "      <td>oil</td>\n",
+       "      <td>GAS</td>\n",
+       "      <td>OIL</td>\n",
        "      <td></td>\n",
        "      <td></td>\n",
        "      <td></td>\n",
@@ -289,8 +289,8 @@
        "      <th>1</th>\n",
        "      <td>nitrogen</td>\n",
        "      <td>8.49998E-4</td>\n",
-       "      <td>8.70757E-4</td>\n",
-       "      <td>1.39448E-6</td>\n",
+       "      <td>8.70763E-4</td>\n",
+       "      <td>1.36793E-6</td>\n",
        "      <td></td>\n",
        "      <td></td>\n",
        "      <td>[mole fraction]</td>\n",
@@ -299,8 +299,8 @@
        "      <th>2</th>\n",
        "      <td>CO2</td>\n",
        "      <td>3.26669E-2</td>\n",
-       "      <td>3.34524E-2</td>\n",
-       "      <td>5.57794E-4</td>\n",
+       "      <td>3.34527E-2</td>\n",
+       "      <td>5.54883E-4</td>\n",
        "      <td></td>\n",
        "      <td></td>\n",
        "      <td>[mole fraction]</td>\n",
@@ -309,8 +309,8 @@
        "      <th>3</th>\n",
        "      <td>methane</td>\n",
        "      <td>8.62505E-1</td>\n",
-       "      <td>8.83475E-1</td>\n",
-       "      <td>5.27028E-3</td>\n",
+       "      <td>8.83482E-1</td>\n",
+       "      <td>5.20781E-3</td>\n",
        "      <td></td>\n",
        "      <td></td>\n",
        "      <td>[mole fraction]</td>\n",
@@ -319,8 +319,8 @@
        "      <th>4</th>\n",
        "      <td>ethane</td>\n",
        "      <td>4.28819E-2</td>\n",
-       "      <td>4.38895E-2</td>\n",
-       "      <td>1.68985E-3</td>\n",
+       "      <td>4.389E-2</td>\n",
+       "      <td>1.68005E-3</td>\n",
        "      <td></td>\n",
        "      <td></td>\n",
        "      <td>[mole fraction]</td>\n",
@@ -392,11 +392,11 @@
       ],
       "text/plain": [
        "           0           1           2           3 4  5                 6\n",
-       "0                  total         gas         oil                       \n",
-       "1   nitrogen  8.49998E-4  8.70757E-4  1.39448E-6        [mole fraction]\n",
-       "2        CO2  3.26669E-2  3.34524E-2  5.57794E-4        [mole fraction]\n",
-       "3    methane  8.62505E-1  8.83475E-1  5.27028E-3        [mole fraction]\n",
-       "4     ethane  4.28819E-2  4.38895E-2  1.68985E-3        [mole fraction]\n",
+       "0                  total         GAS         OIL                       \n",
+       "1   nitrogen  8.49998E-4  8.70763E-4  1.36793E-6        [mole fraction]\n",
+       "2        CO2  3.26669E-2  3.34527E-2  5.54883E-4        [mole fraction]\n",
+       "3    methane  8.62505E-1  8.83482E-1  5.20781E-3        [mole fraction]\n",
+       "4     ethane  4.28819E-2    4.389E-2  1.68005E-3        [mole fraction]\n",
        "..       ...         ...         ...         ... .. ..              ...\n",
        "59    Stream                                                          -\n",
        "60                                                                     \n",
@@ -407,7 +407,7 @@
        "[64 rows x 7 columns]"
       ]
      },
-     "execution_count": 9,
+     "execution_count": 5,
      "metadata": {},
      "output_type": "execute_result"
     }
@@ -419,11 +419,8 @@
   }
  ],
  "metadata": {
-  "interpreter": {
-   "hash": "a5df7bd4ca0d6bb9986d9d69faf4f6c25893f82bf7982e9868ee8495bd8c927f"
-  },
   "kernelspec": {
-   "display_name": "Python 3.7.9 64-bit ('base': conda)",
+   "display_name": "Python 3",
    "language": "python",
    "name": "python3"
   },
@@ -437,7 +434,7 @@
    "name": "python",
    "nbconvert_exporter": "python",
    "pygments_lexer": "ipython3",
-   "version": "3.7.9"
+   "version": "3.10.16"
   },
   "orig_nbformat": 4
  },