♨️ Kalina Binary Cycle (NH3-H2O)

Calculate binary ammonia-water Kalina cycle performance: non-azeotropic temperature glide matching, separator distillation, rich-vapor expander, and net electrical power.

⚡ Fortran 90 Engine Double Precision (IEEE 754) ✓ ISO / ASME Validated
📊 Solver Telemetry ● ACTIVE
👁️ Consultations 40
⚡ Calculs faits 33
💾 Téléchargements 342 📦 Code Fortran 11.4 KB
📅 Mise en service Jun 2026
⏱️ Latence < 1 ms
⚡ Outils & Rapports :
💾 Télécharger Fortran 90

⚡ Kalina Binary (NH3-H2O) Flow Circuit & Variable Boiling Glide

Real-time visual simulation: Distillation separation of rich ammonia vapor and variable-temperature boiling glide

📝 Configuration & Presets

🌋 Geothermal Brine (KCS-11) 🏭 Refinery Distillation Waste 🚛 Gas Engine Bottoming Loop 🌊 OTEC Low-DeltaT Variation
🧪 Binary Mixture Composition & Pressures
Typical: 0.65 to 0.85
⚙️ Mass Flow & Machine Efficiencies
Kalina Binary Cycle Formulation:
• Variable Boiling Temperature Glide: ΔTglide ≈ 15 - 30 °C
• Distillation: Splits into rich vapor (xrich ≈ 95%) and lean liquid (xlean ≈ 40%)
• Net Power Output: Ẇnet = ṁvap · wturb − ṁbasic · wpump [kW]
• Thermal Efficiency: ηth = Ẇnet / Q̇in [%]

📊 Kalina Cycle Results

Configure inputs and click Compute to view results.

📘 Calculation Methodology & Kalina Cycle Standards

Binary Temperature Glide

Because ammonia ($T_b = -33.3^\circ\text{C}$) boils before water ($T_b = 100^\circ\text{C}$), phase change occurs with a variable temperature glide matching the heat source slope, drastically cutting exergy destruction.

Distillation & Absorber Recombination

The high-pressure separator distills rich ammonia vapor for power generation, while lean liquid is recombined in the absorber to allow low condensing pressures at ambient temperature.

Key Engineering Assumptions

  • Zeotropic ammonia-water binary mixture ($NH_3 / H_2O$).
  • Dry rich vapor expansion without condensation in the turbine.
  • Applicable to geothermal power, industrial waste heat recovery, and OTEC.