4.7 Article

Study on a near-zero emission SOFC-based multi-generation system combined with organic Rankine cycle and transcritical CO2 cycle for LNG cold energy recovery

期刊

ENERGY CONVERSION AND MANAGEMENT
卷 253, 期 -, 页码 -

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PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.enconman.2021.115188

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Multi-generation system; SOFC; CO2 capture; LNG; Organic Rankine cycle

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This study proposes a multi-generation system based on solid oxide fuel cells (SOFC), which integrates organic Rankine cycle and transcritical carbon dioxide cycle to achieve near-zero emissions. A liquefied natural gas (LNG) cold energy utilization system is introduced to realize CO2 condensation and capture. The system demonstrates cooperative production of energy and matter, with high thermal efficiency, net electrical efficiency, and exergy efficiency. Exergy analysis reveals the most significant losses occur in the SOFC top cycle. Parameters analysis shows that different operating conditions affect the system's electrical efficiency and exergy efficiency.
This study proposes a near-zero emission SOFC based multi-generation system integrated with organic Rankine cycle and transcritical carbon dioxide cycle, and a LNG cold energy utilization system is also introduced in order to realize CO2 condensation and cryogenic capture. In the proposed system, the unreacted anode gas of SOFC is burned with pure oxygen instead of cathode gas by which it can provide the possibility for the follow-up CO2 capture at low energy consumption assisted by LNG cold energy utilization. The novel poly-generation system can realize the cooperative production of the energy (cooling, heating and power output), and the matter (condensate recovery and captured CO2). The energy and exergy analysis are performed to investigate the proposed system performance based on the established steady-state model. The results reveal that, under the design conditions, the thermal efficiency, net electrical efficiency and exergy efficiency of the proposed system achieve 90.99%, 55.01% and 53.07%, respectively. And the amount of CO2 captured, condensate recovery, and natural gas supply reach 5219.21 ton/year, 1324.83 ton/year and 4273.13 ton/year, respectively. Moreover, the exergy analysis shows that the exergy loss proportion of SOFC top cycle accounts for 47.3% of the total losses. Parameters analysis indicate that the electrical efficiency and the exergy efficiency are increased first and then decreased, and achieve the maximums at the SOFC inlet temperature of 554.4 degrees C and the operating pressure of 650 kPa, respectively. In addition, it is observed that the variation of steam-to-carbon ratio (STCR) has little effect on electrical efficiency and exergy efficiency, but has obvious effect on thermal efficiency. It is also found that the cooling, heating and power output are increased, but all the efficiencies are decreased as current density increases.

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