๐Ÿ”„ Supercritical CO2 Recompression Brayton

Size closed-loop supercritical CO2 (sCO2) recompression Brayton power loops: thermal efficiency (>45%), net electrical power (MW), split recompression ratio, and dual recuperator duties.

โšก Fortran 90 Engine Double Precision (IEEE 754) โœ“ ISO / ASME Validated
Supercritical CO2 Recompression Brayton Thermodynamics
๐Ÿ“Š Solver Telemetry โ— ACTIVE
๐Ÿ‘๏ธ Views 38
โšก Solves 33
๐Ÿ’พ Downloads 452 ๐Ÿ“ฆ Fortran Code 11.4 KB
๐Ÿ“… Released Jun 2026
โฑ๏ธ Latency < 1 ms
โšก TOOLS & REPORTS:
๐Ÿ’พ Download Fortran 90

โš›๏ธ Closed-Loop sCO2 Recompression Power Cycle & Dual Recuperators

Real-time visual simulation: Dense-phase main compressor + bypass recompressor with LTR/HTR heat recovery

๐Ÿ“ Configuration & Presets

โš›๏ธ Gen-IV Nuclear (650ยฐC) โ˜€๏ธ Solar Tower CSP (700ยฐC) ๐Ÿ”ฅ Allam Oxy-Fuel (1100ยฐC) ๐Ÿญ SMR Compact sCO2 (550ยฐC)
โšก Operating Pressures & Temperatures
1 MPa = 10 bar
Near critical point (7.38 MPa)
โš™๏ธ Mass Flow & Split Recompression
Fraction bypassing precooler to RC
sCO2 Recompression Brayton Formulation:
โ€ข Net Cycle Work: wnet = wt โˆ’ (1โˆ’ฮณ)ยทwMC โˆ’ ฮณยทwRC [kJ/kg]
โ€ข Thermal Efficiency: ฮทth = wnet / qheater [%]
โ€ข Dense-phase compression near critical point (ฯ โ‰ˆ 600 kg/mยณ) drastically cuts pump work.
โ€ข Dual recuperators (LTR & HTR) eliminate pinch-point heat exchange mismatch.

๐Ÿ“Š sCO2 Cycle Results

๐Ÿ“Š Output Summary
๐Ÿ’พ Fortran Source

Net Electrical Power Output (Wฬ‡net)
51.06 MW
Thermal Efficiency: 35.64 % | Reactor Duty: 143.2 MW
Phigh = 30 MPa (300 bar)
Gross Turbine Power (Wฬ‡t) 63.53 MW ฮทt = 93 %
Main Compressor Power (MC) 6.06 MW Flow = 72 %
Recompressor Power (RC) 6.41 MW ฮณ = 28 %
Precooler Heat Rejection 92.19 MW Low-temp heat sink

๐Ÿ“ˆ Thermal Efficiency ฮท (%) vs Recompression Fraction ฮณ

๐Ÿ“‰ Net Power Output W_net (MW) vs Turbine Inlet Temp TIT (ยฐC)

=================================================================
 THERMOFLUIDCALC โ€” SUPERCRITICAL CO2 RECOMPRESSION BRAYTON REPORT
=================================================================
Case Title                 : Direct-Fired Oxy-Combustion Allam-Fetvedt Zero-Emission sCO2
Pressure Range             : P_high = 30.00 MPa (300.0 bar), P_low = 8.00 MPa (80.0 bar)
Temperatures & Mass Flow   : TIT = 1100.0 C, MC Inlet = 33.0 C, Total m_dot = 150.0 kg/s
Split Recompression Ratio  : gamma = 0.280 (RC flow = 42.0 kg/s, MC flow = 108.0 kg/s)
-----------------------------------------------------------------
NET ELECTRICAL POWER (Wnet): 51.057 MW (51056.6 kW)
CYCLE THERMAL EFFICIENCY   : 35.642 %
Gross Turbine Power Output : 63.526 MW
Main Compressor Power (MC) : 6.059 MW
Recompressor Power (RC)    : 6.410 MW
Main Heater / Reactor Duty : 143.250 MW
Precooler Heat Rejection   : 92.193 MW
=================================================================

๐Ÿ“˜ Calculation Methodology & sCO2 Brayton Standards

Near-Critical Compression Advantage

Compressing supercritical $CO_2$ just above its critical point ($31.1^\circ\text{C}, 7.38\,\text{MPa}$) exploits high density ($\sim 600\,\text{kg/m}^3$), reducing compressor power consumption by over $60\%$ compared to ideal gases.

Split-Flow Recompression Architecture

The recompression compressor (RC) takes a fraction $\gamma$ of hot low-pressure fluid directly from the LTR outlet without cooling, perfectly matching the specific heat capacitance rates ($mc_p$) across the recuperator.

Key Engineering Assumptions

  • Closed-loop closed Brayton cycle with pure $CO_2$.
  • Dual printed-circuit heat exchangers (PCHE) for LTR and HTR.
  • Applicable to Gen-IV nuclear reactors, solar tower CSP, and waste heat recovery.