Work

Research on semi-closed supercritical CO2 cycle based on mixed-flow direct-contact condensation coupled with density-difference separation

Year: 2026

Type: article

Abstract: The carbon-capture advantage of semi-closed supercritical CO 2 (sCO 2 ) cycles originates from oxy-fuel combustion; however, the additional energy consumption of air separation units (ASU) significantly reduces net system efficiency, necessitating further efficiency improvement. This work proposes an innovative cold-end heat rejection methodology that employs mixed-flow direct-contact condensation between CO 2 and water coupled with density-difference separation, thereby replacing conventional gas–liquid indirect cooling with liquid–liquid cooling. This approach reduces the heat-transfer temperature difference, enables subcritical CO 2 liquefaction, and transitions the compression mechanism from compressor-driven near-critical gas-phase compression to pump-driven liquid-phase compression. The thermophysical feasibility rests on CO 2 –H 2 O mutual solubilities of 25 mol/kmol and 4 mol/kmol, respectively, coupled with a liquid-phase density differential of approximately 260 kg/m 3 across the operating envelope, which together facilitate the coupling of mixed-flow condensation and density-difference separation. A semi-closed sCO 2 cycle incorporating this concept (MSC) is constructed and evaluated. Results demonstrate a cold-end temperature reduction from 32 °C to 27 °C, a 67.35 MW decrease in compression power, a 4.7 percentage-point increase in cycle thermal efficiency to 65.51%, and an improvement in system exergy efficiency from 57.66% to 59.76%. This cold-end-focused study provides a novel technical pathway for performance enhancement of semi-closed CO 2 cycles.

Source: International Communications in Heat and Mass Transfer

DOI: 10.1016/j.icheatmasstransfer.2026.111265