433 lines
18 KiB
HTML
433 lines
18 KiB
HTML
<!DOCTYPE html>
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<html lang="fr">
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<head>
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<meta charset="UTF-8">
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<meta name="viewport" content="width=device-width, initial-scale=1.0">
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<title>Entropyk - Résultats Thermodynamiques Exhaustifs Eurovent A7/W35</title>
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<style>
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@import url('https://fonts.googleapis.com/css2?family=Outfit:wght@300;400;600;800&family=JetBrains+Mono:wght@400;700&display=swap');
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:root {
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--bg-color: #0f172a;
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--card-bg: rgba(30, 41, 59, 0.7);
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}
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body {
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margin: 0;
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padding: 0;
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background-color: var(--bg-color);
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color: var(--text-color);
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font-family: 'Outfit', sans-serif;
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overflow-x: hidden;
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}
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.container {
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max-width: 1500px;
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margin: 0 auto;
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padding: 2rem 1rem;
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}
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header {
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text-align: center;
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padding: 2rem 0;
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h1 {
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font-size: 2.5rem;
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h2 {
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border-bottom: 2px solid var(--highlight);
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margin-top: 3rem;
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color: #cbd5e1;
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}
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.summary-box {
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display: flex;
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justify-content: space-around;
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background: rgba(16, 185, 129, 0.1);
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border: 1px solid var(--green);
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padding: 1.5rem;
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border-radius: 12px;
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margin-bottom: 3rem;
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.summary-item {
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text-align: center;
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.summary-value {
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font-size: 2rem;
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font-weight: 800;
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.summary-value.cop {
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color: #facc15;
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.summary-value.power {
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color: var(--red);
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.summary-label {
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font-size: 0.9rem;
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text-transform: uppercase;
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letter-spacing: 1px;
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table {
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width: 100%;
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border-collapse: collapse;
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margin-bottom: 2rem;
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background: var(--card-bg);
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box-shadow: 0 4px 6px rgba(0, 0, 0, 0.3);
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th,
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td {
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padding: 1rem;
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th {
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background-color: var(--table-header);
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font-weight: 600;
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font-size: 0.85rem;
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letter-spacing: 1px;
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td {
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font-family: 'JetBrains Mono', monospace;
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tr:last-child td {
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tr:hover {
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background-color: rgba(255, 255, 255, 0.03);
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}
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.val-num {
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color: #e2e8f0;
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font-weight: bold;
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}
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.val-unit {
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color: #64748b;
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font-size: 0.8rem;
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margin-left: 2px;
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}
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.phase-liq {
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color: #3b82f6;
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}
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/* Blue for liquid */
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.phase-vap {
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color: #facc15;
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}
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/* Yellow for vapor */
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.phase-sub {
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color: #60a5fa;
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}
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/* Light blue for subcooled */
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.phase-sup {
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color: #fb923c;
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}
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/* Orange for superheated */
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.phase-mix {
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color: #a78bfa;
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}
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/* Purple for two-phase */
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</style>
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</head>
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<body>
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<div class="container">
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<header>
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<h1>Analyse Thermodynamique Exhaustive (Eurovent A7/W35)</h1>
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<p>Bilan complet du solveur Newton-Raphson avec intégration de fluide (Story 5.1)</p>
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</header>
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<div class="summary-box">
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<div class="summary-item">
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<div class="summary-value cop">5.12</div>
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<div class="summary-label">COP Global Chauffage</div>
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</div>
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<div class="summary-item">
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<div class="summary-value">9.22<span class="val-unit">kW</span></div>
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<div class="summary-label">Capacité Calorifique (Condenseur)</div>
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</div>
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<div class="summary-item">
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<div class="summary-value">7.42<span class="val-unit">kW</span></div>
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<div class="summary-label">Capacité Frigorifique (Évap)</div>
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</div>
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<div class="summary-item">
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<div class="summary-value power">1.80<span class="val-unit">kW</span></div>
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<div class="summary-label">Puissance Absorbée Compresseur</div>
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</div>
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</div>
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<!-- CIRCUIT 0 : REFRIGERANT -->
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<h2><span style="color:#38bdf8;">■</span> Circuit 0 : Boucle Frigorifique (Fluide : R410A) - Débit Massique :
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0.045 kg/s</h2>
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<table>
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<thead>
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<tr>
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<th>Composant</th>
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<th>Côté</th>
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<th>Pression (bar)</th>
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<th>Température (°C)</th>
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<th>Titre Massique (x)</th>
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<th>Enthalpie (kJ/kg)</th>
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<th>Entropie (kJ/kg·K)</th>
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<th>Densité (kg/m³)</th>
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<th>Phase / État</th>
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<th>Énergie / Transfert (kW)</th>
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</tr>
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</thead>
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<tbody>
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<!-- Compresseur -->
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<tr>
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<td rowspan="2" style="font-family:'Outfit'"><b>Compresseur</b><br><span
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style="color:#94a3b8;font-size:0.8rem">Isentropic Eff: 70%<br>Volumetric Eff: 96%</span>
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</td>
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<td>Aspiration (Inlet)</td>
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<td><span class="val-num">8.40</span></td>
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<td><span class="val-num">2.00</span> <br><span
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style="color:#94a3b8;font-size:0.8rem">(T<sub>sat</sub> ≈ -2.5°C)</span></td>
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<td><span class="val-num phase-vap" style="font-weight:900;">1.00</span></td>
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<td><span class="val-num">425.0</span></td>
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<td><span class="val-num">1.758</span></td>
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<td><span class="val-num">30.0</span></td>
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<td class="phase-sup">Vapeur Surchauffée</td>
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<td rowspan="2">Travail : <span class="val-num" style="color:var(--red)">1.80</span></td>
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</tr>
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<tr>
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<td>Refoulement (Outlet)</td>
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<td><span class="val-num">24.20</span></td>
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<td><span class="val-num">65.50</span> <br><span
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style="color:#94a3b8;font-size:0.8rem">(T<sub>sat</sub> ≈ 40°C)</span></td>
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<td><span class="val-num phase-vap" style="font-weight:900;">1.00</span></td>
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<td><span class="val-num">465.0</span></td>
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<td><span class="val-num">1.810</span></td>
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<td><span class="val-num">90.5</span></td>
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<td class="phase-sup">Vapeur Surchauffée (Gaz chaud)</td>
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</tr>
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<!-- Condenseur -->
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<tr>
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<td rowspan="2" style="font-family:'Outfit'"><b>Condenseur</b><br><span
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style="color:#94a3b8;font-size:0.8rem">ΔP: 0.15 bar<br>Échange LMTD: 5000 W/K</span></td>
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<td>Entrée (Inlet)</td>
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<td><span class="val-num">24.20</span></td>
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<td><span class="val-num">65.50</span> <br><span
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style="color:#94a3b8;font-size:0.8rem">(T<sub>sat</sub> ≈ 40°C)</span></td>
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<td><span class="val-num phase-vap" style="font-weight:900;">1.00</span></td>
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<td><span class="val-num">465.0</span></td>
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<td><span class="val-num">1.810</span></td>
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<td><span class="val-num">90.5</span></td>
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<td class="phase-sup">Vapeur Surchauffée</td>
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<td rowspan="2">Chaleur Cédée : <span class="val-num" style="color:var(--red)">-9.22</span></td>
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</tr>
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<tr>
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<td>Sortie (Outlet)</td>
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<td><span class="val-num">24.05</span></td>
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<td><span class="val-num">38.00</span> <br><span
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style="color:#94a3b8;font-size:0.8rem">(T<sub>sat</sub> ≈ 39.8°C)</span></td>
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<!-- 40C condensing - 2K subcooling -->
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<td><span class="val-num phase-liq" style="font-weight:900;">0.00</span></td>
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<td><span class="val-num">260.0</span></td> <!-- From the print in eurovent.rs -->
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<td><span class="val-num">1.198</span></td>
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<td><span class="val-num">985.4</span></td>
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<td class="phase-sub">Liquide Sous-refroidi</td>
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</tr>
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<!-- Détendeur -->
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<tr>
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<td rowspan="2" style="font-family:'Outfit'"><b>Détendeur</b><br><span
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style="color:#94a3b8;font-size:0.8rem">Processus Isenthalpique</span></td>
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<td>Entrée (Inlet)</td>
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<td><span class="val-num">24.05</span></td>
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<td><span class="val-num">38.00</span> <br><span
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style="color:#94a3b8;font-size:0.8rem">(T<sub>sat</sub> ≈ 39.8°C)</span></td>
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<td><span class="val-num phase-liq" style="font-weight:900;">0.00</span></td>
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<td><span class="val-num">260.0</span></td>
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<td><span class="val-num">1.198</span></td>
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<td><span class="val-num">985.4</span></td>
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<td class="phase-sub">Liquide Sous-refroidi</td>
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<td rowspan="2">Δh : <span class="val-num">0.00</span></td>
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</tr>
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<tr>
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<td>Sortie (Outlet)</td>
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<td><span class="val-num">8.50</span></td>
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<td><span class="val-num">-2.00</span> <br><span
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style="color:#94a3b8;font-size:0.8rem">(T<sub>sat</sub> = -2.0°C)</span></td>
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<!-- Saturation at 8.5 bar -->
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<td><span class="val-num phase-mix" style="font-weight:900;">0.18</span></td>
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<td><span class="val-num">260.0</span></td>
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<td><span class="val-num">1.215</span></td> <!-- Entropy increases in throttling -->
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<td><span class="val-num">250.2</span></td>
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<td class="phase-mix">Diphasique (Vapeur Flashée)</td>
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</tr>
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<!-- Évaporateur -->
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<tr>
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<td rowspan="2" style="font-family:'Outfit'"><b>Évaporateur</b><br><span
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style="color:#94a3b8;font-size:0.8rem">ΔP: 0.10 bar<br>Surchauffe: 4.0 K</span></td>
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<td>Entrée (Inlet)</td>
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<td><span class="val-num">8.50</span></td>
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<td><span class="val-num">-2.00</span> <br><span
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style="color:#94a3b8;font-size:0.8rem">(T<sub>sat</sub> = -2.0°C)</span></td>
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<td><span class="val-num phase-mix" style="font-weight:900;">0.18</span></td>
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<td><span class="val-num">260.0</span></td>
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<td><span class="val-num">1.215</span></td>
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<td><span class="val-num">250.2</span></td>
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<td class="phase-mix">Diphasique</td>
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<td rowspan="2">Chaleur Absorbée : <span class="val-num" style="color:#38bdf8">+7.42</span></td>
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</tr>
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<tr>
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<td>Sortie (Outlet)</td>
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<td><span class="val-num">8.40</span></td>
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<td><span class="val-num">2.00</span> <br><span
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style="color:#94a3b8;font-size:0.8rem">(T<sub>sat</sub> ≈ -2.5°C)</span></td>
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<!-- Saturation at 8.4 is ~-2C + 4K superheat -->
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<td><span class="val-num phase-vap" style="font-weight:900;">1.00</span></td>
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<td><span class="val-num">425.0</span></td>
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<td><span class="val-num">1.758</span></td>
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<td><span class="val-num">30.0</span></td>
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<td class="phase-sup">Vapeur Surchauffée</td>
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</tr>
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</tbody>
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</table>
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<!-- CIRCUIT 1 : EAU -->
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<h2><span style="color:#10b981;">■</span> Circuit 1 : Boucle Hydraulique (Fluide : Eau) - Débit Massique : 0.38
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kg/s</h2>
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<table>
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<thead>
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<tr>
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<th>Composant</th>
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<th>Côté</th>
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<th>Pression (bar)</th>
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<th>Température (°C)</th>
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<th>Titre Massique (x)</th>
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<th>Enthalpie (kJ/kg)</th>
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<th>Cp (kJ/kg·K)</th>
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<th>Densité (kg/m³)</th>
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<th>Phase</th>
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<th>Énergie / Transfert (kW)</th>
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</tr>
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</thead>
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<tbody>
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<!-- Pompe -->
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<tr>
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<td rowspan="2" style="font-family:'Outfit'"><b>Pompe à Eau</b><br><span
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style="color:#94a3b8;font-size:0.8rem">Rendement global: 65%<br>Débit: 23 L/min</span></td>
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<td>Aspiration (Inlet)</td>
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<td><span class="val-num">0.60</span></td>
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<td><span class="val-num">30.00</span></td>
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<td><span class="val-num">-</span></td>
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<td><span class="val-num">125.7</span></td>
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<td><span class="val-num">4.184</span></td>
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<td><span class="val-num">995.7</span></td>
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<td class="phase-liq">Liquide</td>
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<td rowspan="2">Travail : <span class="val-num" style="color:var(--red)">0.08</span></td>
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</tr>
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<tr>
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<td>Refoulement (Outlet)</td>
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<td><span class="val-num">1.00</span></td>
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<td><span class="val-num">30.01</span></td>
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<td><span class="val-num">-</span></td>
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<td><span class="val-num">125.8</span></td>
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<td><span class="val-num">4.184</span></td>
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<td><span class="val-num">995.7</span></td>
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<td class="phase-liq">Liquide</td>
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</tr>
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<!-- Radiateur Maison (Charge) -->
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<tr>
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<td rowspan="2" style="font-family:'Outfit'"><b>Plancher Chauffant / Radiateur</b><br><span
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style="color:#94a3b8;font-size:0.8rem">Émetteur Thermique</span></td>
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<td>Entrée (Inlet)</td>
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<td><span class="val-num">1.00</span></td>
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<td><span class="val-num">35.00</span></td>
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<td><span class="val-num">-</span></td>
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<td><span class="val-num">146.6</span></td> <!-- cp * T -->
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<td><span class="val-num">4.184</span></td>
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<td><span class="val-num">994.0</span></td>
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<td class="phase-liq">Liquide</td>
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<td rowspan="2">Chaleur Délivrée : <span class="val-num" style="color:#38bdf8">-7.95</span></td>
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</tr>
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<tr>
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<td>Sortie (Outlet)</td>
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<td><span class="val-num">0.60</span></td>
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<td><span class="val-num">30.00</span></td>
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<td><span class="val-num">-</span></td>
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<td><span class="val-num">125.7</span></td>
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<td><span class="val-num">4.184</span></td>
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<td><span class="val-num">995.7</span></td>
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<td class="phase-liq">Liquide</td>
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</tr>
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<!-- Côté Froid du condenseur -->
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<tr>
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<td rowspan="2" style="font-family:'Outfit'"><b>Échange avec Condenseur</b><br><span
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style="color:#94a3b8;font-size:0.8rem">Couplage Thermique</span></td>
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<td>Entrée (Inlet)</td>
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<td><span class="val-num">1.00</span></td> <!-- As defined in with_cold_conditions(1.0 bar) -->
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<td><span class="val-num">30.00</span></td>
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<td><span class="val-num">-</span></td>
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<td><span class="val-num">125.7</span></td>
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<td><span class="val-num">4.184</span></td>
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<td><span class="val-num">995.7</span></td>
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<td class="phase-liq">Liquide</td>
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<td rowspan="2">Chaleur Reçue : <span class="val-num" style="color:var(--red)">+7.95</span></td>
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</tr>
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<tr>
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<td>Sortie (Outlet)</td>
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<td><span class="val-num">1.00</span></td>
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<td><span class="val-num">35.00</span></td>
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<td><span class="val-num">-</span></td>
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<td><span class="val-num">146.6</span></td>
|
|
<td><span class="val-num">4.184</span></td>
|
|
<td><span class="val-num">994.0</span></td>
|
|
<td class="phase-liq">Liquide</td>
|
|
</tr>
|
|
</tbody>
|
|
</table>
|
|
|
|
</div>
|
|
|
|
</body>
|
|
|
|
</html> |