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Property Estimation
-
Property
-
Temperature
-K
Pressure
-kPa
Temperature Dependence
T_min: K
T_max: K
Distillation Column Design
-
Condenser Reboiler Feed F = 100 Distillate D = 40 Bottoms B = 60
Theoretical Stages
-
Feed Stage
-
Reflux Ratio
-
Column Diameter
-m
EquipmentHeat Duty
Condenser (Qc)-
Reboiler (Qr)-
Mass Balance Analysis
-
Process Unit Closure: --% Feed - mol/s Distillate - mol/s Bottoms - mol/s
Mass Closure
-%
Heat Balance Analysis
-
Heat Exchanger 熱交換器 Inlet T = 300 K Outlet T = 400 K Q = 0 kW
Sensible Heat
-kW
Latent Heat
-kW
Total Duty
-kW
Actual Duty
-kW
Phase InformationValue
Inlet Phase-
Outlet Phase-
Boiling Point-
Phase Change-
Liquid-Liquid Extraction
-
Extraction Column Feed (F) 100 kmol/h Solvent (S) 50 kmol/h Raffinate (R) - kmol/h Extract (E) - kmol/h
Recovery / 抽出率
-%
Stages / 段数
-
Extraction Factor (E)
-
Distribution Coef (m)
-
StreamFlow (kmol/h)Solute Composition
Feed--
Solvent--
Raffinate--
Extract--
Gas Absorption Tower
-
Absorption Tower Gas In 100 kmol/h Gas Out - kmol/h Liquid In Liquid Out - kmol/h
Removal / 除去率
-%
Stages / 段数
-
Absorption Factor (A)
-
L/G Ratio
-
StreamFlow (kmol/h)Composition
Gas In--
Gas Out--
Liquid In--
Liquid Out--
Absorbed Amount / 吸収量
-kmol/h
LCOH (水素製造原価)
PEM Electrolysis
Levelized Cost of Hydrogen
- EUR/kg H₂
Cost Breakdown / コスト内訳
Annual Production / 年間生産量
-ton/year
Total CAPEX / 総投資額
-M EUR
Energy Efficiency / エネルギー効率
-%
CO₂ Intensity / CO₂排出原単位
-kg/kg H₂
Cost Component / コスト項目EUR/kg H₂Share / 割合
CAPEX (設備投資)--
Energy (エネルギー)--
OPEX (運転費・基礎)--
Labor (人件費)--
Maintenance (保守費)--
Stack Replacement (スタック交換)--
Water (水)--
Carbon Cost (炭素コスト)--
Revenue/Subsidy (収益/補助)--
Sensitivity Analysis / 感度分析
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