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Numerical simulation of condensation heat transfer outside low pressure CO2/H2O horizontal tube bundle
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Fengyan CAO1, Junhui LU1, Hongbing CHEN1, Yan WANG2, Suilin WANG1
Thermal Power Generation | 2025, 54(3) : 69 - 78
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Thermal Power Generation | 2025, 54(3): 69-78
Thermal energy science research
Numerical simulation of condensation heat transfer outside low pressure CO2/H2O horizontal tube bundle
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Fengyan CAO1, Junhui LU1, Hongbing CHEN1, Yan WANG2, Suilin WANG1
Affiliations
  • 1.School of Environment and Energy Engineering, Beijing University of Civil Engineering and Architecture, Beijing 100044, China
  • 2.National Key Laboratory of Spacecraft Thermal Control, General Design Department of Beijing Space Vehicle, Beijing 100094, China
Published: 2025-03-25 doi: 10.19666/j.rlfd.202407201
Outline
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Carbon capture and storage is an important way to achieve the “dual-carbon” goal. The exhaust gas of the supercritical water-coal to hydrogen coupled CO2/H2O mixed working medium thermal power generation system is low pressure and low-temperature CO2/H2O mixed gas. In order to achieve zero carbon emission and heat recovery, condensation separation of CO2/H2O is a necessary way. Fluent is used to simulate the condensing heat transfer characteristics of CO2/H2O mixture outside the horizontal bifurcation tube bundle. The volume of fluid (VOF) model, the component transport model, and the phase transition model written by the user-defined functions (UDF) are employed to load the mass, energy, and component source terms of the two-phase flow. The formation and development process of the liquid film on the wall surface, and the distribution of streamlines, velocity vectors, and liquid-phase volume fractions in the vicinity of droplets, as well as the effects of velocity, vapor superheat, and noncondensable gas content on the heat transfer coefficients and the thermal resistance of the diffusion layer, are investigated. The results show that, the simulation results are in agreement with the experimental data, and the liquid film thermal resistance hardly varies with the steam superheat but decreases with the increase of CO2 content, inlet flow rate and total pressure. The thermal resistance of the mixed gas diffusion layer increases with the CO2 content and steam superheat, and decreases with the increase of inlet flow rate. The total heat transfer coefficient increases with the steam superheat, inlet flow rate and pressure, and decreases with the CO2 content, and the local condensation heat transfer coefficient is negatively correlated with the liquid film thickness. A new dimensionless correlation formula for heat and mass transfer of condensation is proposed for low pressure CO2/H2O condensation process.

numerical simulation  /  CO2/H2O mixture gas  /  low pressure  /  forklift tube bundle  /  condensation heat transfer
Fengyan CAO, Junhui LU, Hongbing CHEN, Yan WANG, Suilin WANG. Numerical simulation of condensation heat transfer outside low pressure CO2/H2O horizontal tube bundle[J]. Thermal Power Generation, 2025 , 54 (3) : 69 -78 . DOI: 10.19666/j.rlfd.202407201
Year 2025 volume 54 Issue 3
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doi: 10.19666/j.rlfd.202407201
  • Receive Date:2024-07-25
  • Online Date:2026-03-06
  • Published:2025-03-25
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  • Received:2024-07-25
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Affiliations
    1.School of Environment and Energy Engineering, Beijing University of Civil Engineering and Architecture, Beijing 100044, China
    2.National Key Laboratory of Spacecraft Thermal Control, General Design Department of Beijing Space Vehicle, Beijing 100094, China
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表12种不同金属材料的力学参数

Family
属数
Number of
genus
种数
Number of
species
占总种数比例
Percentage of
total species (%)

Genus
种数
Number of
species
占总种数比例
Percentage of total
species (%)
鹅膏菌科Amanitaceae 2 11 5.26 鹅膏菌属 Amanita 10 4.78
小菇科 Mycenaceae 2 12 5.74 丝盖伞属 Inocybe 5 2.39
多孔菌科 Polyporaceae 8 14 6.70 蜡蘑属 Laccaria 5 2.39
红菇科 Russulaceae 3 23 11.00 小皮伞属 Marasmius 6 2.87
小菇属 Mycena 11 5.26
光柄菇属 Pluteus 5 2.39
红菇属 Russula 17 8.13
栓菌属 Trametes 5 2.39
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