chore: remove deprecated flow_boundary and update docs to match new architecture
This commit is contained in:
Sepehr
@@ -25,7 +25,7 @@
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"outputs": [],
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"source": [
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"import entropyk\n",
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"import numpy as np"
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"import numpy as np\n"
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]
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},
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{
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@@ -175,11 +175,25 @@
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"except entropyk.SolverError as e:\n",
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" print(\"Solver error:\", e)\n"
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]
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"metadata": {},
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"outputs": [],
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"source": []
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"metadata": {},
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"outputs": [],
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"source": []
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}
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],
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"metadata": {
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"kernelspec": {
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"display_name": "Python 3",
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"display_name": "entropyk",
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"language": "python",
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"name": "python3"
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},
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@@ -17,7 +17,7 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 1,
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"metadata": {},
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"outputs": [],
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"source": [
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@@ -39,9 +39,20 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 2,
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"metadata": {},
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"outputs": [],
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"outputs": [
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{
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"name": "stdout",
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"output_type": "stream",
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"text": [
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"Pression:\n",
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" 1200000.00 Pa → 12.00 bar, 1200.0 kPa, 174.0 psi\n",
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" 350000.00 Pa → 3.50 bar\n",
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" 1034213.59 Pa → 10.34 bar\n"
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]
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}
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],
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"source": [
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"# Pression - plusieurs unités supportées\n",
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"p1 = entropyk.Pressure(bar=12.0)\n",
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@@ -56,9 +67,20 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 3,
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"metadata": {},
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"outputs": [],
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"outputs": [
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{
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"name": "stdout",
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"output_type": "stream",
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"text": [
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"Température:\n",
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" 318.15 K → 45.00°C, 113.00°F\n",
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" 273.15 K → 0.00°C (point de congélation)\n",
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" 310.93 K → 37.78°C, 310.93 K\n"
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]
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}
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],
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"source": [
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"# Température\n",
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"t1 = entropyk.Temperature(celsius=45.0)\n",
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@@ -73,9 +95,19 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 4,
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"metadata": {},
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"outputs": [],
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"outputs": [
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{
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"name": "stdout",
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"output_type": "stream",
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"text": [
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"Enthalpie:\n",
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" 420000.00 J/kg → 420.0 kJ/kg\n",
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" 250000.00 J/kg → 250.0 kJ/kg\n"
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]
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}
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],
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"source": [
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"# Enthalpie\n",
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"h1 = entropyk.Enthalpy(kj_per_kg=420.0)\n",
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@@ -88,9 +120,19 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 5,
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"metadata": {},
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"outputs": [],
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"outputs": [
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{
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"name": "stdout",
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"output_type": "stream",
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"text": [
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"Débit massique:\n",
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" 0.050000 kg/s → 50.0 g/s\n",
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" 0.050000 kg/s → 0.0500 kg/s\n"
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]
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}
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],
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"source": [
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"# Débit massique\n",
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"m1 = entropyk.MassFlow(kg_per_s=0.05)\n",
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@@ -112,7 +154,7 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 6,
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"metadata": {},
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"outputs": [],
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"source": [
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@@ -149,9 +191,22 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 7,
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"metadata": {},
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"outputs": [],
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"outputs": [
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{
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"name": "stdout",
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"output_type": "stream",
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"text": [
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"Cycles HFC classiques:\n",
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"--------------------------------------------------\n",
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" R134a → 8 variables d'état\n",
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" R410A → 8 variables d'état\n",
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" R407C → 8 variables d'état\n",
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" R32 → 8 variables d'état\n"
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]
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}
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],
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"source": [
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"# Test avec différents fluides HFC classiques\n",
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"hfc_fluids = [\"R134a\", \"R410A\", \"R407C\", \"R32\"]\n",
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@@ -174,9 +229,114 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 8,
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"metadata": {},
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"outputs": [],
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"outputs": [
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{
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"data": {
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"text/html": [
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"<div>\n",
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"<style scoped>\n",
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" .dataframe tbody tr th:only-of-type {\n",
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" vertical-align: middle;\n",
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" }\n",
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"\n",
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" .dataframe tbody tr th {\n",
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" vertical-align: top;\n",
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" }\n",
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"\n",
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" .dataframe thead th {\n",
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" text-align: right;\n",
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" }\n",
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"</style>\n",
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"<table border=\"1\" class=\"dataframe\">\n",
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" <thead>\n",
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" <tr style=\"text-align: right;\">\n",
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" <th></th>\n",
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" <th>Fluide</th>\n",
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" <th>Type</th>\n",
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" <th>GWP</th>\n",
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" <th>Usage</th>\n",
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" </tr>\n",
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" </thead>\n",
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" <tbody>\n",
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" <tr>\n",
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" <th>0</th>\n",
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" <td>R1234yf</td>\n",
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" <td>HFO</td>\n",
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" <td><1</td>\n",
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" <td>Remplacement R134a (automobile)</td>\n",
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" </tr>\n",
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" <tr>\n",
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" <th>1</th>\n",
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" <td>R1234ze(E)</td>\n",
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" <td>HFO</td>\n",
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" <td><1</td>\n",
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" <td>Remplacement R134a (stationnaire)</td>\n",
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" </tr>\n",
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" <tr>\n",
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" <th>2</th>\n",
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" <td>R1233zd(E)</td>\n",
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" <td>HCFO</td>\n",
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" <td>1</td>\n",
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" <td>Remplacement R123 (basse pression)</td>\n",
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" </tr>\n",
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" <tr>\n",
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" <th>3</th>\n",
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" <td>R1243zf</td>\n",
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" <td>HFO</td>\n",
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" <td><1</td>\n",
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" <td>Nouveau fluide recherche</td>\n",
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" </tr>\n",
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" <tr>\n",
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" <th>4</th>\n",
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" <td>R1336mzz(E)</td>\n",
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" <td>HFO</td>\n",
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" <td><1</td>\n",
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" <td>ORC, haute température</td>\n",
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" </tr>\n",
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" <tr>\n",
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" <th>5</th>\n",
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" <td>R513A</td>\n",
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" <td>Mélange</td>\n",
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" <td>631</td>\n",
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" <td>R134a + R1234yf (56/44)</td>\n",
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" </tr>\n",
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" <tr>\n",
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" <th>6</th>\n",
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" <td>R454B</td>\n",
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" <td>Mélange</td>\n",
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" <td>146</td>\n",
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" <td>R32 + R1234yf (50/50) - Opteon XL41</td>\n",
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" </tr>\n",
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" <tr>\n",
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" <th>7</th>\n",
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" <td>R452B</td>\n",
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" <td>Mélange</td>\n",
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" <td>676</td>\n",
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" <td>R32 + R125 + R1234yf - Opteon XL55</td>\n",
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" </tr>\n",
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" </tbody>\n",
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"</table>\n",
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"</div>"
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],
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"text/plain": [
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" Fluide Type GWP Usage\n",
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"0 R1234yf HFO <1 Remplacement R134a (automobile)\n",
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"1 R1234ze(E) HFO <1 Remplacement R134a (stationnaire)\n",
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"2 R1233zd(E) HCFO 1 Remplacement R123 (basse pression)\n",
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"3 R1243zf HFO <1 Nouveau fluide recherche\n",
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"4 R1336mzz(E) HFO <1 ORC, haute température\n",
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"5 R513A Mélange 631 R134a + R1234yf (56/44)\n",
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"6 R454B Mélange 146 R32 + R1234yf (50/50) - Opteon XL41\n",
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"7 R452B Mélange 676 R32 + R125 + R1234yf - Opteon XL55"
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]
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},
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"execution_count": 8,
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"metadata": {},
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"output_type": "execute_result"
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}
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],
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"source": [
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"# HFO et alternatives Low-GWP\n",
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"low_gwp_fluids = [\n",
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@@ -196,9 +356,26 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 9,
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"metadata": {},
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"outputs": [],
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"outputs": [
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{
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"name": "stdout",
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"output_type": "stream",
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"text": [
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"Cycles HFO / Low-GWP:\n",
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"--------------------------------------------------\n",
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" R1234yf → ✅ Supporté (8 vars)\n",
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" R1234ze(E) → ✅ Supporté (8 vars)\n",
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" R1233zd(E) → ✅ Supporté (8 vars)\n",
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" R1243zf → ✅ Supporté (8 vars)\n",
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" R1336mzz(E) → ✅ Supporté (8 vars)\n",
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" R513A → ✅ Supporté (8 vars)\n",
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" R454B → ✅ Supporté (8 vars)\n",
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" R452B → ✅ Supporté (8 vars)\n"
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]
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}
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],
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"source": [
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"# Test cycles HFO\n",
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"print(\"Cycles HFO / Low-GWP:\")\n",
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@@ -222,9 +399,98 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 10,
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"metadata": {},
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"outputs": [],
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"outputs": [
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{
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"data": {
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"text/html": [
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"<div>\n",
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"<style scoped>\n",
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" .dataframe tbody tr th:only-of-type {\n",
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" vertical-align: middle;\n",
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" }\n",
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"\n",
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" .dataframe tbody tr th {\n",
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" vertical-align: top;\n",
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" }\n",
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"\n",
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" .dataframe thead th {\n",
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" text-align: right;\n",
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" }\n",
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"</style>\n",
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"<table border=\"1\" class=\"dataframe\">\n",
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" <thead>\n",
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" <tr style=\"text-align: right;\">\n",
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" <th></th>\n",
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" <th>Code ASHRAE</th>\n",
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" <th>Nom</th>\n",
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" <th>GWP</th>\n",
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" <th>Application</th>\n",
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" </tr>\n",
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" </thead>\n",
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" <tbody>\n",
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" <tr>\n",
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" <th>0</th>\n",
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" <td>R744</td>\n",
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" <td>CO2</td>\n",
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" <td>1</td>\n",
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" <td>Transcritique, commercial</td>\n",
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" </tr>\n",
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" <tr>\n",
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" <th>1</th>\n",
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" <td>R290</td>\n",
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" <td>Propane</td>\n",
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" <td>3</td>\n",
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" <td>Climatisation, commercial</td>\n",
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" </tr>\n",
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" <tr>\n",
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" <th>2</th>\n",
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" <td>R600a</td>\n",
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" <td>Isobutane</td>\n",
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" <td>3</td>\n",
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" <td>Domestique, commerc. faible charge</td>\n",
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" </tr>\n",
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" <tr>\n",
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" <th>3</th>\n",
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" <td>R600</td>\n",
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" <td>Butane</td>\n",
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" <td>3</td>\n",
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" <td>Réfrigération basse température</td>\n",
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" </tr>\n",
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" <tr>\n",
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" <th>4</th>\n",
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" <td>R1270</td>\n",
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" <td>Propylène</td>\n",
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" <td>3</td>\n",
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" <td>Climatisation industrielle</td>\n",
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" </tr>\n",
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" <tr>\n",
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" <th>5</th>\n",
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" <td>R717</td>\n",
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" <td>Ammonia</td>\n",
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" <td>0</td>\n",
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" <td>Industriel, forte puissance</td>\n",
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" </tr>\n",
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" </tbody>\n",
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"</table>\n",
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"</div>"
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],
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"text/plain": [
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" Code ASHRAE Nom GWP Application\n",
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"0 R744 CO2 1 Transcritique, commercial\n",
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"1 R290 Propane 3 Climatisation, commercial\n",
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"2 R600a Isobutane 3 Domestique, commerc. faible charge\n",
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"3 R600 Butane 3 Réfrigération basse température\n",
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"4 R1270 Propylène 3 Climatisation industrielle\n",
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"5 R717 Ammonia 0 Industriel, forte puissance"
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]
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},
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"execution_count": 10,
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"metadata": {},
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"output_type": "execute_result"
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}
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],
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"source": [
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"# Fluides naturels\n",
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"natural_fluids = [\n",
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@@ -242,9 +508,24 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 11,
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"metadata": {},
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"outputs": [],
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"outputs": [
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{
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"name": "stdout",
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"output_type": "stream",
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"text": [
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"Cycles fluides naturels:\n",
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"--------------------------------------------------\n",
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" R744 (CO2 ) → ✅ Supporté\n",
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" R290 (Propane ) → ✅ Supporté\n",
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" R600a (Isobutane ) → ✅ Supporté\n",
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" R600 (Butane ) → ✅ Supporté\n",
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" R1270 (Propylène ) → ✅ Supporté\n",
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" R717 (Ammonia ) → ✅ Supporté\n"
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]
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}
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],
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"source": [
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"# Test cycles fluides naturels\n",
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"print(\"Cycles fluides naturels:\")\n",
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@@ -266,9 +547,17 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 12,
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"metadata": {},
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"outputs": [],
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"outputs": [
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{
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"name": "stdout",
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"output_type": "stream",
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"text": [
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"Total réfrigérants classiques: 26\n"
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]
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}
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],
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"source": [
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"# Autres réfrigérants disponibles\n",
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"other_refrigerants = [\n",
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@@ -295,9 +584,168 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 13,
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"metadata": {},
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"outputs": [],
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"outputs": [
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{
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"data": {
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"text/html": [
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||||
"<div>\n",
|
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"<style scoped>\n",
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||||
" .dataframe tbody tr th:only-of-type {\n",
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||||
" vertical-align: middle;\n",
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" }\n",
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"\n",
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||||
" .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>Nom CoolProp</th>\n",
|
||||
" <th>Formule</th>\n",
|
||||
" <th>Usage</th>\n",
|
||||
" </tr>\n",
|
||||
" </thead>\n",
|
||||
" <tbody>\n",
|
||||
" <tr>\n",
|
||||
" <th>0</th>\n",
|
||||
" <td>Water</td>\n",
|
||||
" <td>H2O</td>\n",
|
||||
" <td>Fluide de travail, calibration</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>1</th>\n",
|
||||
" <td>Air</td>\n",
|
||||
" <td>N2+O2</td>\n",
|
||||
" <td>Climatisation, psychrométrie</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>2</th>\n",
|
||||
" <td>Nitrogen</td>\n",
|
||||
" <td>N2</td>\n",
|
||||
" <td>Cryogénie, inertage</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>3</th>\n",
|
||||
" <td>Oxygen</td>\n",
|
||||
" <td>O2</td>\n",
|
||||
" <td>Applications spéciales</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>4</th>\n",
|
||||
" <td>Argon</td>\n",
|
||||
" <td>Ar</td>\n",
|
||||
" <td>Cryogénie</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>5</th>\n",
|
||||
" <td>Helium</td>\n",
|
||||
" <td>He</td>\n",
|
||||
" <td>Cryogénie très basse T</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>6</th>\n",
|
||||
" <td>Hydrogen</td>\n",
|
||||
" <td>H2</td>\n",
|
||||
" <td>Énergie, cryogénie</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>7</th>\n",
|
||||
" <td>Methane</td>\n",
|
||||
" <td>CH4</td>\n",
|
||||
" <td>GNL, pétrole</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>8</th>\n",
|
||||
" <td>Ethane</td>\n",
|
||||
" <td>C2H6</td>\n",
|
||||
" <td>Pétrochimie</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>9</th>\n",
|
||||
" <td>Ethylene</td>\n",
|
||||
" <td>C2H4</td>\n",
|
||||
" <td>Pétrochimie</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>10</th>\n",
|
||||
" <td>Propane</td>\n",
|
||||
" <td>C3H8</td>\n",
|
||||
" <td>= R290</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>11</th>\n",
|
||||
" <td>Butane</td>\n",
|
||||
" <td>C4H10</td>\n",
|
||||
" <td>= R600</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>12</th>\n",
|
||||
" <td>Ethanol</td>\n",
|
||||
" <td>C2H5OH</td>\n",
|
||||
" <td>Solvant</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>13</th>\n",
|
||||
" <td>Methanol</td>\n",
|
||||
" <td>CH3OH</td>\n",
|
||||
" <td>Solvant</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>14</th>\n",
|
||||
" <td>Acetone</td>\n",
|
||||
" <td>C3H6O</td>\n",
|
||||
" <td>Solvant</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>15</th>\n",
|
||||
" <td>Benzene</td>\n",
|
||||
" <td>C6H6</td>\n",
|
||||
" <td>Chimie</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>16</th>\n",
|
||||
" <td>Toluene</td>\n",
|
||||
" <td>C7H8</td>\n",
|
||||
" <td>ORC</td>\n",
|
||||
" </tr>\n",
|
||||
" </tbody>\n",
|
||||
"</table>\n",
|
||||
"</div>"
|
||||
],
|
||||
"text/plain": [
|
||||
" Nom CoolProp Formule Usage\n",
|
||||
"0 Water H2O Fluide de travail, calibration\n",
|
||||
"1 Air N2+O2 Climatisation, psychrométrie\n",
|
||||
"2 Nitrogen N2 Cryogénie, inertage\n",
|
||||
"3 Oxygen O2 Applications spéciales\n",
|
||||
"4 Argon Ar Cryogénie\n",
|
||||
"5 Helium He Cryogénie très basse T\n",
|
||||
"6 Hydrogen H2 Énergie, cryogénie\n",
|
||||
"7 Methane CH4 GNL, pétrole\n",
|
||||
"8 Ethane C2H6 Pétrochimie\n",
|
||||
"9 Ethylene C2H4 Pétrochimie\n",
|
||||
"10 Propane C3H8 = R290\n",
|
||||
"11 Butane C4H10 = R600\n",
|
||||
"12 Ethanol C2H5OH Solvant\n",
|
||||
"13 Methanol CH3OH Solvant\n",
|
||||
"14 Acetone C3H6O Solvant\n",
|
||||
"15 Benzene C6H6 Chimie\n",
|
||||
"16 Toluene C7H8 ORC"
|
||||
]
|
||||
},
|
||||
"execution_count": 13,
|
||||
"metadata": {},
|
||||
"output_type": "execute_result"
|
||||
}
|
||||
],
|
||||
"source": [
|
||||
"# Fluides non-réfrigérants disponibles\n",
|
||||
"other_fluids = [\n",
|
||||
@@ -333,9 +781,108 @@
|
||||
},
|
||||
{
|
||||
"cell_type": "code",
|
||||
"execution_count": null,
|
||||
"execution_count": 14,
|
||||
"metadata": {},
|
||||
"outputs": [],
|
||||
"outputs": [
|
||||
{
|
||||
"name": "stdout",
|
||||
"output_type": "stream",
|
||||
"text": [
|
||||
"\n",
|
||||
"=== RÉSUMÉ DES FLUIDES DISPONIBLES ===\n",
|
||||
"Total: 61+ fluides\n",
|
||||
"\n"
|
||||
]
|
||||
},
|
||||
{
|
||||
"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>Catégorie</th>\n",
|
||||
" <th>Exemples</th>\n",
|
||||
" <th>Nombre</th>\n",
|
||||
" </tr>\n",
|
||||
" </thead>\n",
|
||||
" <tbody>\n",
|
||||
" <tr>\n",
|
||||
" <th>0</th>\n",
|
||||
" <td>HFC Classiques</td>\n",
|
||||
" <td>R134a, R410A, R407C, R32, R125</td>\n",
|
||||
" <td>5</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>1</th>\n",
|
||||
" <td>HFO / Low-GWP</td>\n",
|
||||
" <td>R1234yf, R1234ze(E), R1233zd(E)</td>\n",
|
||||
" <td>6</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>2</th>\n",
|
||||
" <td>Alternatives (Mélanges)</td>\n",
|
||||
" <td>R513A, R454B, R452B, R507A</td>\n",
|
||||
" <td>4</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>3</th>\n",
|
||||
" <td>Fluides Naturels</td>\n",
|
||||
" <td>R744 (CO2), R290, R600a, R717</td>\n",
|
||||
" <td>6</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>4</th>\n",
|
||||
" <td>CFC/HCFC (Obsolètes)</td>\n",
|
||||
" <td>R11, R12, R22, R123, R141b</td>\n",
|
||||
" <td>8</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>5</th>\n",
|
||||
" <td>Autres HFC</td>\n",
|
||||
" <td>R143a, R152A, R227EA, R245fa</td>\n",
|
||||
" <td>15</td>\n",
|
||||
" </tr>\n",
|
||||
" <tr>\n",
|
||||
" <th>6</th>\n",
|
||||
" <td>Non-Réfrigérants</td>\n",
|
||||
" <td>Water, Air, Nitrogen, Helium</td>\n",
|
||||
" <td>17</td>\n",
|
||||
" </tr>\n",
|
||||
" </tbody>\n",
|
||||
"</table>\n",
|
||||
"</div>"
|
||||
],
|
||||
"text/plain": [
|
||||
" Catégorie Exemples Nombre\n",
|
||||
"0 HFC Classiques R134a, R410A, R407C, R32, R125 5\n",
|
||||
"1 HFO / Low-GWP R1234yf, R1234ze(E), R1233zd(E) 6\n",
|
||||
"2 Alternatives (Mélanges) R513A, R454B, R452B, R507A 4\n",
|
||||
"3 Fluides Naturels R744 (CO2), R290, R600a, R717 6\n",
|
||||
"4 CFC/HCFC (Obsolètes) R11, R12, R22, R123, R141b 8\n",
|
||||
"5 Autres HFC R143a, R152A, R227EA, R245fa 15\n",
|
||||
"6 Non-Réfrigérants Water, Air, Nitrogen, Helium 17"
|
||||
]
|
||||
},
|
||||
"execution_count": 14,
|
||||
"metadata": {},
|
||||
"output_type": "execute_result"
|
||||
}
|
||||
],
|
||||
"source": [
|
||||
"# Catégorisation complète\n",
|
||||
"fluid_summary = {\n",
|
||||
@@ -377,9 +924,24 @@
|
||||
},
|
||||
{
|
||||
"cell_type": "code",
|
||||
"execution_count": null,
|
||||
"execution_count": 15,
|
||||
"metadata": {},
|
||||
"outputs": [],
|
||||
"outputs": [
|
||||
{
|
||||
"name": "stdout",
|
||||
"output_type": "stream",
|
||||
"text": [
|
||||
"=== Cycle CO2 Transcritique (R744) ===\n",
|
||||
"\n",
|
||||
"Propriétés du CO2:\n",
|
||||
" Point critique: 31.0°C, 73.8 bar\n",
|
||||
" GWP: 1\n",
|
||||
" Applications: Supermarchés, transports, chaleur industrielle\n",
|
||||
"\n",
|
||||
"Système créé: 8 variables d'état\n"
|
||||
]
|
||||
}
|
||||
],
|
||||
"source": [
|
||||
"# Cycle CO2 transcritique\n",
|
||||
"print(\"=== Cycle CO2 Transcritique (R744) ===\")\n",
|
||||
@@ -401,9 +963,25 @@
|
||||
},
|
||||
{
|
||||
"cell_type": "code",
|
||||
"execution_count": null,
|
||||
"execution_count": 16,
|
||||
"metadata": {},
|
||||
"outputs": [],
|
||||
"outputs": [
|
||||
{
|
||||
"name": "stdout",
|
||||
"output_type": "stream",
|
||||
"text": [
|
||||
"=== Cycle Ammoniac (R717) ===\n",
|
||||
"\n",
|
||||
"Propriétés de l'Ammoniac:\n",
|
||||
" Point critique: 132.4°C, 113.3 bar\n",
|
||||
" GWP: 0 (naturel)\n",
|
||||
" haute efficacité, toxique mais détectable\n",
|
||||
" Applications: Industrie agroalimentaire, patinoires, entrepôts\n",
|
||||
"\n",
|
||||
"Système créé: 8 variables d'état\n"
|
||||
]
|
||||
}
|
||||
],
|
||||
"source": [
|
||||
"# Cycle Ammoniac\n",
|
||||
"print(\"=== Cycle Ammoniac (R717) ===\")\n",
|
||||
@@ -426,9 +1004,26 @@
|
||||
},
|
||||
{
|
||||
"cell_type": "code",
|
||||
"execution_count": null,
|
||||
"execution_count": 17,
|
||||
"metadata": {},
|
||||
"outputs": [],
|
||||
"outputs": [
|
||||
{
|
||||
"name": "stdout",
|
||||
"output_type": "stream",
|
||||
"text": [
|
||||
"=== Cycle Propane (R290) ===\n",
|
||||
"\n",
|
||||
"Propriétés du Propane:\n",
|
||||
" Point critique: 96.7°C, 42.5 bar\n",
|
||||
" GWP: 3 (très bas)\n",
|
||||
" Excellentes propriétés thermodynamiques\n",
|
||||
" Inflammable (A3)\n",
|
||||
" Applications: Climatisation, pompes à chaleur, commercial\n",
|
||||
"\n",
|
||||
"Système créé: 8 variables d'état\n"
|
||||
]
|
||||
}
|
||||
],
|
||||
"source": [
|
||||
"# Cycle Propane\n",
|
||||
"print(\"=== Cycle Propane (R290) ===\")\n",
|
||||
@@ -452,9 +1047,17 @@
|
||||
},
|
||||
{
|
||||
"cell_type": "code",
|
||||
"execution_count": null,
|
||||
"execution_count": 18,
|
||||
"metadata": {},
|
||||
"outputs": [],
|
||||
"outputs": [
|
||||
{
|
||||
"name": "stdout",
|
||||
"output_type": "stream",
|
||||
"text": [
|
||||
"Solver configuré: FallbackConfig(newton=NewtonConfig(max_iter=200, tol=1.0e-6, line_search=true), picard=PicardConfig(max_iter=500, tol=1.0e-4, relax=0.50))\n"
|
||||
]
|
||||
}
|
||||
],
|
||||
"source": [
|
||||
"# Exemple de configuration du solveur pour résolution\n",
|
||||
"system = build_simple_cycle(\"R134a\")\n",
|
||||
@@ -502,7 +1105,7 @@
|
||||
],
|
||||
"metadata": {
|
||||
"kernelspec": {
|
||||
"display_name": "Python 3",
|
||||
"display_name": "entropyk",
|
||||
"language": "python",
|
||||
"name": "python3"
|
||||
},
|
||||
@@ -516,7 +1119,7 @@
|
||||
"name": "python",
|
||||
"nbconvert_exporter": "python",
|
||||
"pygments_lexer": "ipython3",
|
||||
"version": "3.11.0"
|
||||
"version": "3.13.11"
|
||||
}
|
||||
},
|
||||
"nbformat": 4,
|
||||
|
||||
@@ -214,6 +214,60 @@
|
||||
"## 5. Recommandations par Application"
|
||||
]
|
||||
},
|
||||
{
|
||||
"cell_type": "code",
|
||||
"execution_count": null,
|
||||
"metadata": {},
|
||||
"outputs": [],
|
||||
"source": [
|
||||
"import entropyk\n",
|
||||
"\n",
|
||||
"# Create a system\n",
|
||||
"system = entropyk.System()\n",
|
||||
"\n",
|
||||
"# Add components\n",
|
||||
"# Note: Python bindings use simplified adapters for demonstration\n",
|
||||
"compressor = entropyk.Compressor(\n",
|
||||
" speed_rpm=2900.0,\n",
|
||||
" displacement=0.0001, # m³/rev\n",
|
||||
" efficiency=0.85,\n",
|
||||
" fluid=\"R134a\",\n",
|
||||
")\n",
|
||||
"\n",
|
||||
"condenser = entropyk.Condenser(ua=5000.0) # UA in W/K\n",
|
||||
"evaporator = entropyk.Evaporator(ua=3000.0)\n",
|
||||
"valve = entropyk.ExpansionValve(fluid=\"R134a\", opening=0.8)\n",
|
||||
"\n",
|
||||
"# Add to system\n",
|
||||
"comp_idx = system.add_component(compressor)\n",
|
||||
"cond_idx = system.add_component(condenser)\n",
|
||||
"evap_idx = system.add_component(evaporator)\n",
|
||||
"valve_idx = system.add_component(valve)\n",
|
||||
"\n",
|
||||
"# Connect refrigerant circuit\n",
|
||||
"system.add_edge(comp_idx, cond_idx) # Compressor → Condenser (hot side)\n",
|
||||
"system.add_edge(cond_idx, valve_idx) # Condenser → Valve\n",
|
||||
"system.add_edge(valve_idx, evap_idx) # Valve → Evaporator (cold side)\n",
|
||||
"system.add_edge(evap_idx, comp_idx) # Evaporator → Compressor\n",
|
||||
"\n",
|
||||
"# Finalize topology\n",
|
||||
"system.finalize()\n",
|
||||
"\n",
|
||||
"# Configure solver\n",
|
||||
"solver = entropyk.NewtonConfig(\n",
|
||||
" max_iterations=200,\n",
|
||||
" tolerance=1e-6,\n",
|
||||
" line_search=True,\n",
|
||||
")\n",
|
||||
"\n",
|
||||
"# Solve (requires proper boundary conditions and fluid backend)\n",
|
||||
"try:\n",
|
||||
" result = solver.solve(system)\n",
|
||||
" print(f\"Converged in {result.iterations} iterations\")\n",
|
||||
"except entropyk.SolverError as e:\n",
|
||||
" print(f\"Solver error: {e}\")\n"
|
||||
]
|
||||
},
|
||||
{
|
||||
"cell_type": "code",
|
||||
"execution_count": null,
|
||||
@@ -294,15 +348,28 @@
|
||||
},
|
||||
{
|
||||
"cell_type": "code",
|
||||
"execution_count": null,
|
||||
"execution_count": 2,
|
||||
"metadata": {},
|
||||
"outputs": [],
|
||||
"outputs": [
|
||||
{
|
||||
"ename": "NameError",
|
||||
"evalue": "name 'entropyk' is not defined",
|
||||
"output_type": "error",
|
||||
"traceback": [
|
||||
"\u001b[31m---------------------------------------------------------------------------\u001b[39m",
|
||||
"\u001b[31mNameError\u001b[39m Traceback (most recent call last)",
|
||||
"\u001b[36mCell\u001b[39m\u001b[36m \u001b[39m\u001b[32mIn[2]\u001b[39m\u001b[32m, line 48\u001b[39m\n\u001b[32m 46\u001b[39m \u001b[38;5;66;03m# Test\u001b[39;00m\n\u001b[32m 47\u001b[39m \u001b[38;5;28;01mfor\u001b[39;00m fluid \u001b[38;5;129;01min\u001b[39;00m [\u001b[33m\"\u001b[39m\u001b[33mR134a\u001b[39m\u001b[33m\"\u001b[39m, \u001b[33m\"\u001b[39m\u001b[33mR32\u001b[39m\u001b[33m\"\u001b[39m, \u001b[33m\"\u001b[39m\u001b[33mR290\u001b[39m\u001b[33m\"\u001b[39m, \u001b[33m\"\u001b[39m\u001b[33mR744\u001b[39m\u001b[33m\"\u001b[39m]:\n\u001b[32m---> \u001b[39m\u001b[32m48\u001b[39m system = \u001b[43mcreate_cycle_for_fluid\u001b[49m\u001b[43m(\u001b[49m\u001b[43mfluid\u001b[49m\u001b[43m,\u001b[49m\u001b[43m \u001b[49m\u001b[33;43m\"\u001b[39;49m\u001b[33;43mClimatisation\u001b[39;49m\u001b[33;43m\"\u001b[39;49m\u001b[43m)\u001b[49m\n\u001b[32m 49\u001b[39m \u001b[38;5;28mprint\u001b[39m(\u001b[33mf\u001b[39m\u001b[33m\"\u001b[39m\u001b[38;5;132;01m{\u001b[39;00mfluid\u001b[38;5;132;01m:\u001b[39;00m\u001b[33m8s\u001b[39m\u001b[38;5;132;01m}\u001b[39;00m\u001b[33m: \u001b[39m\u001b[38;5;132;01m{\u001b[39;00msystem.state_vector_len\u001b[38;5;132;01m}\u001b[39;00m\u001b[33m variables d\u001b[39m\u001b[33m'\u001b[39m\u001b[33métat\u001b[39m\u001b[33m\"\u001b[39m)\n",
|
||||
"\u001b[36mCell\u001b[39m\u001b[36m \u001b[39m\u001b[32mIn[2]\u001b[39m\u001b[32m, line 21\u001b[39m, in \u001b[36mcreate_cycle_for_fluid\u001b[39m\u001b[34m(fluid, app_name)\u001b[39m\n\u001b[32m 18\u001b[39m ua_cond = \u001b[32m5000.0\u001b[39m\n\u001b[32m 19\u001b[39m ua_evap = \u001b[32m3000.0\u001b[39m\n\u001b[32m---> \u001b[39m\u001b[32m21\u001b[39m system = \u001b[43mentropyk\u001b[49m.System()\n\u001b[32m 23\u001b[39m comp = entropyk.Compressor(\n\u001b[32m 24\u001b[39m speed_rpm=\u001b[32m2900.0\u001b[39m,\n\u001b[32m 25\u001b[39m displacement=\u001b[32m0.0001\u001b[39m,\n\u001b[32m 26\u001b[39m efficiency=\u001b[32m0.85\u001b[39m,\n\u001b[32m 27\u001b[39m fluid=fluid\n\u001b[32m 28\u001b[39m )\n\u001b[32m 29\u001b[39m cond = entropyk.Condenser(ua=ua_cond)\n",
|
||||
"\u001b[31mNameError\u001b[39m: name 'entropyk' is not defined"
|
||||
]
|
||||
}
|
||||
],
|
||||
"source": [
|
||||
"def create_cycle_for_fluid(fluid: str, app_name: str = \"Climatisation\"):\n",
|
||||
" \"\"\"\n",
|
||||
" Crée un cycle optimisé pour un fluide et une application donnée.\n",
|
||||
" \"\"\"\n",
|
||||
" params = applications[app_name]\n",
|
||||
" #params = applications[app_name]\n",
|
||||
" \n",
|
||||
" # Ajuster les composants selon le fluide\n",
|
||||
" if fluid == \"R744\":\n",
|
||||
@@ -349,6 +416,253 @@
|
||||
" print(f\"{fluid:8s}: {system.state_vector_len} variables d'état\")"
|
||||
]
|
||||
},
|
||||
{
|
||||
"cell_type": "code",
|
||||
"execution_count": 1,
|
||||
"metadata": {},
|
||||
"outputs": [
|
||||
{
|
||||
"name": "stdout",
|
||||
"output_type": "stream",
|
||||
"text": [
|
||||
"Construction du système Entropyk complet...\n",
|
||||
"Finalisation du graphe (Construction de la topologie)...\n",
|
||||
"Propriétés du système : 18 composants, 17 connexions.\n",
|
||||
"Taille du vecteur d'état mathématique : 34 variables.\n",
|
||||
"\n",
|
||||
"Configuration de la stratégie de résolution...\n",
|
||||
"Lancement de la simulation (Newton uniquement)...\n",
|
||||
"\n",
|
||||
"❌ Erreur du solveur : Solver diverged: Jacobian is singular - cannot solve linear system\n",
|
||||
"Note: Ce comportement peut arriver si les paramètres (taille des tuyaux, coeffs, températures)\n",
|
||||
"dépassent le domaine thermodynamique du fluide ou si le graphe manque de contraintes aux limites.\n"
|
||||
]
|
||||
}
|
||||
],
|
||||
"source": [
|
||||
"import entropyk\n",
|
||||
"import math\n",
|
||||
"\n",
|
||||
"def build_complete_system():\n",
|
||||
" # ── 1. Initialisation du graphe du système ──\n",
|
||||
" system = entropyk.System()\n",
|
||||
" print(\"Construction du système Entropyk complet...\")\n",
|
||||
"\n",
|
||||
" # Paramètres fluides\n",
|
||||
" refrigerant = \"R410A\"\n",
|
||||
" water = \"Water\"\n",
|
||||
"\n",
|
||||
" # =========================================================================\n",
|
||||
" # BOUCLE 1 : CIRCUIT FRIGORIFIQUE (REFRIGERANT R410A)\n",
|
||||
" # =========================================================================\n",
|
||||
" \n",
|
||||
" # 1.1 Compresseur (Modèle Polynomial AHRI 540)\n",
|
||||
" compressor = system.add_component(entropyk.Compressor(\n",
|
||||
" m1=0.85, m2=2.5, m3=500.0, m4=1500.0, m5=-2.5, m6=1.8, m7=600.0, m8=1600.0, m9=-3.0, m10=2.0,\n",
|
||||
" speed_rpm=3600.0,\n",
|
||||
" displacement=0.00008,\n",
|
||||
" efficiency=0.88,\n",
|
||||
" fluid=refrigerant\n",
|
||||
" ))\n",
|
||||
" \n",
|
||||
" # 1.2 Tuyau de refoulement (vers condenseur)\n",
|
||||
" pipe_hot = system.add_component(entropyk.Pipe(\n",
|
||||
" length=5.0,\n",
|
||||
" diameter=0.02,\n",
|
||||
" fluid=refrigerant\n",
|
||||
" ))\n",
|
||||
" \n",
|
||||
" # 1.3 Condenseur (Rejet de chaleur)\n",
|
||||
" condenser = system.add_component(entropyk.Condenser(\n",
|
||||
" ua=4500.0,\n",
|
||||
" fluid=refrigerant,\n",
|
||||
" water_temp=30.0, # Température d'entrée côté eau/air\n",
|
||||
" water_flow=2.0\n",
|
||||
" ))\n",
|
||||
" \n",
|
||||
" # 1.4 Ligne liquide\n",
|
||||
" pipe_liquid = system.add_component(entropyk.Pipe(\n",
|
||||
" length=10.0,\n",
|
||||
" diameter=0.015,\n",
|
||||
" fluid=refrigerant\n",
|
||||
" ))\n",
|
||||
" \n",
|
||||
" # 1.5 Division du débit (FlowSplitter) vers 2 évaporateurs\n",
|
||||
" splitter = system.add_component(entropyk.FlowSplitter(n_outlets=2))\n",
|
||||
" \n",
|
||||
" # 1.6 Branche A : Détendeur + Évaporateur 1\n",
|
||||
" exv_a = system.add_component(entropyk.ExpansionValve(fluid=refrigerant, opening=0.5))\n",
|
||||
" evap_a = system.add_component(entropyk.Evaporator(\n",
|
||||
" ua=2000.0,\n",
|
||||
" fluid=refrigerant,\n",
|
||||
" water_temp=12.0,\n",
|
||||
" water_flow=1.0\n",
|
||||
" ))\n",
|
||||
" \n",
|
||||
" # 1.7 Branche B : Détendeur + Évaporateur 2\n",
|
||||
" exv_b = system.add_component(entropyk.ExpansionValve(fluid=refrigerant, opening=0.5))\n",
|
||||
" evap_b = system.add_component(entropyk.Evaporator(\n",
|
||||
" ua=2000.0,\n",
|
||||
" fluid=refrigerant,\n",
|
||||
" water_temp=15.0, # Température d'eau légèrement différente\n",
|
||||
" water_flow=1.0\n",
|
||||
" ))\n",
|
||||
" \n",
|
||||
" # 1.8 Fusion du débit (FlowMerger)\n",
|
||||
" merger = system.add_component(entropyk.FlowMerger(n_inlets=2))\n",
|
||||
" \n",
|
||||
" # 1.9 Tuyau d'aspiration (retour compresseur)\n",
|
||||
" pipe_suction = system.add_component(entropyk.Pipe(\n",
|
||||
" length=5.0,\n",
|
||||
" diameter=0.025,\n",
|
||||
" fluid=refrigerant\n",
|
||||
" ))\n",
|
||||
"\n",
|
||||
" # --- Connexions de la boucle frigo ---\n",
|
||||
" system.add_edge(compressor, pipe_hot)\n",
|
||||
" system.add_edge(pipe_hot, condenser)\n",
|
||||
" system.add_edge(condenser, pipe_liquid)\n",
|
||||
" \n",
|
||||
" # Splitter\n",
|
||||
" system.add_edge(pipe_liquid, splitter)\n",
|
||||
" system.add_edge(splitter, exv_a)\n",
|
||||
" system.add_edge(splitter, exv_b)\n",
|
||||
" \n",
|
||||
" # Branches parallèles\n",
|
||||
" system.add_edge(exv_a, evap_a)\n",
|
||||
" system.add_edge(exv_b, evap_b)\n",
|
||||
" \n",
|
||||
" # Merger\n",
|
||||
" system.add_edge(evap_a, merger)\n",
|
||||
" system.add_edge(evap_b, merger)\n",
|
||||
" \n",
|
||||
" system.add_edge(merger, pipe_suction)\n",
|
||||
" system.add_edge(pipe_suction, compressor)\n",
|
||||
"\n",
|
||||
" # =========================================================================\n",
|
||||
" # BOUCLE 2 : CIRCUIT RÉSEAU HYDRAULIQUE (EAU - Côté Évaporateur Principal)\n",
|
||||
" # (Juste de la tuyauterie et une pompe pour montrer les FlowSource/FlowSink)\n",
|
||||
" # =========================================================================\n",
|
||||
" \n",
|
||||
" water_source = system.add_component(entropyk.FlowSource(\n",
|
||||
" fluid=water,\n",
|
||||
" pressure_pa=101325.0, # 1 atm\n",
|
||||
" temperature_k=285.15 # 12 °C\n",
|
||||
" ))\n",
|
||||
" \n",
|
||||
" water_pump = system.add_component(entropyk.Pump(\n",
|
||||
" pressure_rise_pa=50000.0, # 0.5 bar\n",
|
||||
" efficiency=0.6\n",
|
||||
" ))\n",
|
||||
" \n",
|
||||
" water_pipe = system.add_component(entropyk.Pipe(\n",
|
||||
" length=20.0,\n",
|
||||
" diameter=0.05,\n",
|
||||
" fluid=water\n",
|
||||
" ))\n",
|
||||
" \n",
|
||||
" water_sink = system.add_component(entropyk.FlowSink())\n",
|
||||
" \n",
|
||||
" # --- Connexions Hydrauliques Principales ---\n",
|
||||
" system.add_edge(water_source, water_pump)\n",
|
||||
" system.add_edge(water_pump, water_pipe)\n",
|
||||
" system.add_edge(water_pipe, water_sink)\n",
|
||||
"\n",
|
||||
"\n",
|
||||
" # =========================================================================\n",
|
||||
" # BOUCLE 3 : CIRCUIT VENTILATION (AIR - Côté Condenseur)\n",
|
||||
" # =========================================================================\n",
|
||||
" \n",
|
||||
" air_source = system.add_component(entropyk.FlowSource(\n",
|
||||
" fluid=\"Air\",\n",
|
||||
" pressure_pa=101325.0,\n",
|
||||
" temperature_k=308.15 # 35 °C d'air ambiant\n",
|
||||
" ))\n",
|
||||
" \n",
|
||||
" condenser_fan = system.add_component(entropyk.Fan(\n",
|
||||
" pressure_rise_pa=200.0, # 200 Pa de montée en pression par le ventilo\n",
|
||||
" efficiency=0.5\n",
|
||||
" ))\n",
|
||||
" \n",
|
||||
" air_sink = system.add_component(entropyk.FlowSink())\n",
|
||||
" \n",
|
||||
" # --- Connexions Ventilation ---\n",
|
||||
" system.add_edge(air_source, condenser_fan)\n",
|
||||
" system.add_edge(condenser_fan, air_sink)\n",
|
||||
"\n",
|
||||
"\n",
|
||||
" # ── 4. Finalisation du système ──\n",
|
||||
" print(\"Finalisation du graphe (Construction de la topologie)...\")\n",
|
||||
" system.finalize()\n",
|
||||
" print(f\"Propriétés du système : {system.node_count} composants, {system.edge_count} connexions.\")\n",
|
||||
" print(f\"Taille du vecteur d'état mathématique : {system.state_vector_len} variables.\")\n",
|
||||
" \n",
|
||||
" return system\n",
|
||||
"\n",
|
||||
"\n",
|
||||
"def solve_system(system):\n",
|
||||
" # ── 5. Configuration Avancée du Solveur (Story 6-6) ──\n",
|
||||
" print(\"\\nConfiguration de la stratégie de résolution...\")\n",
|
||||
"\n",
|
||||
" # (Optionnel) Critères de convergence fins\n",
|
||||
" convergence = entropyk.ConvergenceCriteria(\n",
|
||||
" pressure_tolerance_pa=5.0,\n",
|
||||
" mass_balance_tolerance_kgs=1e-6,\n",
|
||||
" energy_balance_tolerance_w=1e-3\n",
|
||||
" )\n",
|
||||
"\n",
|
||||
" # (Optionnel) Jacobian Freezing pour aller plus vite\n",
|
||||
" freezing = entropyk.JacobianFreezingConfig(\n",
|
||||
" max_frozen_iters=4,\n",
|
||||
" threshold=0.1\n",
|
||||
" )\n",
|
||||
"\n",
|
||||
" # Configuration Newton avec tolérances avancées\n",
|
||||
" newton_config = entropyk.NewtonConfig(\n",
|
||||
" max_iterations=150,\n",
|
||||
" tolerance=1e-5,\n",
|
||||
" line_search=True,\n",
|
||||
" use_numerical_jacobian=True,\n",
|
||||
" jacobian_freezing=freezing,\n",
|
||||
" convergence_criteria=convergence,\n",
|
||||
" initial_state=[1000000.0, 450000.0] * 17\n",
|
||||
" )\n",
|
||||
"\n",
|
||||
" # Configuration Picard robuste en cas d'échec de Newton\n",
|
||||
" picard_config = entropyk.PicardConfig(\n",
|
||||
" max_iterations=500,\n",
|
||||
" tolerance=1e-4,\n",
|
||||
" relaxation=0.4,\n",
|
||||
" convergence_criteria=convergence\n",
|
||||
" )\n",
|
||||
"\n",
|
||||
" # ── 6. Lancement du calcul ──\n",
|
||||
" print(\"Lancement de la simulation (Newton uniquement)...\")\n",
|
||||
" try:\n",
|
||||
" result = newton_config.solve(system)\n",
|
||||
" \n",
|
||||
" status = result.status\n",
|
||||
" print(f\"\\n✅ Simulation terminée avec succès !\")\n",
|
||||
" print(f\"Statut : {status}\")\n",
|
||||
" print(f\"Itérations : {result.iterations}\")\n",
|
||||
" print(f\"Résidu final : {result.final_residual:.2e}\")\n",
|
||||
" \n",
|
||||
" # Le résultat contient le vecteur d'état complet\n",
|
||||
" state_vec = result.state_vector\n",
|
||||
" print(f\"Aperçu des 5 premières variables d'état : {state_vec[:5]}\")\n",
|
||||
" \n",
|
||||
" except entropyk.TimeoutError:\n",
|
||||
" print(\"\\n❌ Le solveur a dépassé le temps imparti (Timeout).\")\n",
|
||||
" except entropyk.SolverError as e:\n",
|
||||
" print(f\"\\n❌ Erreur du solveur : {e}\")\n",
|
||||
" print(\"Note: Ce comportement peut arriver si les paramètres (taille des tuyaux, coeffs, températures)\")\n",
|
||||
" print(\"dépassent le domaine thermodynamique du fluide ou si le graphe manque de contraintes aux limites.\")\n",
|
||||
"\n",
|
||||
"if __name__ == \"__main__\":\n",
|
||||
" system = build_complete_system()\n",
|
||||
" solve_system(system)\n"
|
||||
]
|
||||
},
|
||||
{
|
||||
"cell_type": "markdown",
|
||||
"metadata": {},
|
||||
@@ -387,7 +701,7 @@
|
||||
],
|
||||
"metadata": {
|
||||
"kernelspec": {
|
||||
"display_name": "Python 3",
|
||||
"display_name": "entropyk",
|
||||
"language": "python",
|
||||
"name": "python3"
|
||||
},
|
||||
@@ -401,7 +715,7 @@
|
||||
"name": "python",
|
||||
"nbconvert_exporter": "python",
|
||||
"pygments_lexer": "ipython3",
|
||||
"version": "3.11.0"
|
||||
"version": "3.13.11"
|
||||
}
|
||||
},
|
||||
"nbformat": 4,
|
||||
|
||||
@@ -549,6 +549,7 @@ impl PyNewtonConfig {
|
||||
initial_state: self.initial_state.clone(),
|
||||
convergence_criteria: self.convergence_criteria.as_ref().map(|cc| cc.inner.clone()),
|
||||
jacobian_freezing: self.jacobian_freezing.as_ref().map(|jf| jf.inner.clone()),
|
||||
verbose_config: Default::default(),
|
||||
};
|
||||
|
||||
// Catch any Rust panic to prevent it from reaching Python (Task 5.4)
|
||||
@@ -739,6 +740,7 @@ impl PyFallbackConfig {
|
||||
initial_state: self.newton.initial_state.clone(),
|
||||
convergence_criteria: self.newton.convergence_criteria.as_ref().map(|cc| cc.inner.clone()),
|
||||
jacobian_freezing: self.newton.jacobian_freezing.as_ref().map(|jf| jf.inner.clone()),
|
||||
verbose_config: Default::default(),
|
||||
};
|
||||
let picard_config = entropyk_solver::PicardConfig {
|
||||
max_iterations: self.picard.max_iterations,
|
||||
@@ -982,6 +984,7 @@ impl PySolverStrategy {
|
||||
initial_state: py_config.initial_state.clone(),
|
||||
convergence_criteria: py_config.convergence_criteria.as_ref().map(|cc| cc.inner.clone()),
|
||||
jacobian_freezing: py_config.jacobian_freezing.as_ref().map(|jf| jf.inner.clone()),
|
||||
verbose_config: Default::default(),
|
||||
};
|
||||
Ok(PySolverStrategy {
|
||||
inner: entropyk_solver::SolverStrategy::NewtonRaphson(config),
|
||||
|
||||
Reference in New Issue
Block a user