Techno-economic and carbon footprint feasibility assessment for polygeneration process of carbon-capture coal-to-methanol/power and molten carbonate fuel cell

被引:36
作者
Li, Mingxin [1 ,3 ]
Zhuang, Yu [1 ,2 ]
Song, Mengting [1 ]
Li, Weida [1 ]
Du, Jian [1 ]
机构
[1] Dalian Univ Technol, Sch Chem Engn, Inst Proc Syst Engn, Dalian 116024, Liaoning, Peoples R China
[2] Dalian Univ Technol, Sch Energy & Power Engn, Key Lab Liaoning Prov Desalinat, Dalian 116024, Liaoning, Peoples R China
[3] Nucl Power Inst China, Res Inst 4, Chengdu 610200, Sichuan, Peoples R China
基金
中国博士后科学基金; 中国国家自然科学基金;
关键词
Coal; Polygeneration; MCFC; Power generation; Methanol synthesis; FIRED POWER-PLANT; CO2; CAPTURE; IGCC SYSTEM; GASIFICATION; CYCLE; PERFORMANCE; INTEGRATION; SIMULATION; DESIGN; GAS;
D O I
10.1016/j.enconman.2021.114015
中图分类号
O414.1 [热力学];
学科分类号
摘要
Coal-based chemical production processes bring severe greenhouse gas emissions. As a significant clean and energy-efficient technology, the polygeneration process has attracted increasing attentions due to its higher energy efficiency, lower production cost and fewer emissions. Towards this end, this work aims to develop a novel coal-based polygeneration process of carbon-capture coal-to-methanol/power and molten carbonate fuel cell (CTMP-MCFC). In the proposed process, coal is first converted to crude syngas. Afterwards, one part of the crude gas is shifted to H2-rich gas, where a part of H2-rich gas goes into the anode of MCFC, and another part of the H2-rich gas mixed with the rest of unshifted syngas goes into the methanol synthesis (MS) unit. The unreacted syngas out of the MS is then sent into the gas turbine (GT) for power generation. The exhausted gas out of the GT goes into the cathode of MCFC for CO2 and O2 supply and CO2 is enriched to the anode for carbon capture simultaneously. Ultimately, waste heat recovery steam cycle at three levels is proposed for global waste heat recovery. An extended pinch-based Duran-Grossmann (D-G) model is introduced to optimize the waste heat utilization. Sensitivity analysis is conducted to investigate the interactive effects of key parameters in MCFC. A comprehensive techno-economic and carbon footprint performance assessment is performed to verify the feasibility of the proposed polygeneration process. Compared with the base plant, carbon footprint shows the great ability to reduce carbon emissions of the proposed system. The product cost of CTMP-MCFC is 12.47 $/GJ and reduced by 1.68%. The exergy efficiency of CTMP-MCFC is improved by 8.53% and the units with the maximum exergy losses are also identified for further energy conservation. The derived significant contributions of this work highlight strong potentials for the overall performance enhancement via an MCFC-integrated polygeneration process.
引用
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页数:13
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共 38 条
[1]   Integration of biomass-fueled power plant and MCFC-cryogenic CO2 separation unit for low-carbon power production: Thermodynamic and exergoeconomic comparative analysis [J].
Akrami, Ehsan ;
Ameri, Mohammad ;
Rocco, Matteo, V .
ENERGY CONVERSION AND MANAGEMENT, 2020, 223
[2]   A modelling approach to the techno-economics of Biomass-to-SNG/Methanol systems: Standalone vs Integrated topologies [J].
Arteaga-Perez, Luis E. ;
Gomez-Capiro, Oscar ;
Karelovic, Alejandro ;
Jimenez, Romel .
CHEMICAL ENGINEERING JOURNAL, 2016, 286 :663-678
[3]   Numerical investigation of a MCFC (Molten Carbonate Fuel Cell) system hybridized with a supercritical CO2 Brayton cycle and compared with a bottoming Organic Rankine Cycle [J].
Baronci, Andrea ;
Messina, Giuseppe ;
McPhail, Stephen J. ;
Moreno, Angelo .
ENERGY, 2015, 93 :1063-1073
[4]   Using MCFC for high efficiency CO2 capture from natural gas combined cycles: Comparison of internal and external reforming [J].
Campanari, Stefano ;
Manzolini, Giampaolo ;
Chiesa, Paolo .
APPLIED ENERGY, 2013, 112 :772-783
[5]   CO2 capture from combined cycles integrated with Molten Carbonate Fuel Cells [J].
Campanari, Stefano ;
Chiesa, Paolo ;
Manzolini, Giampaolo .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2010, 4 (03) :441-451
[6]   Performance of integrated gasification combined cycle power plants integrated with methanol synthesis processes [J].
Carapellucci, R ;
Cau, G ;
Cocco, D .
PROCEEDINGS OF THE INSTITUTION OF MECHANICAL ENGINEERS PART A-JOURNAL OF POWER AND ENERGY, 2001, 215 (A3) :347-356
[7]   The retrofitting of a coal-fired subcritical steam power plant for carbon dioxide capture: A comparison between MCFC-based active systems and conventional MEA [J].
Carapellucci, Roberto ;
Di Battista, Davide ;
Cipollone, Roberto .
ENERGY CONVERSION AND MANAGEMENT, 2019, 194 :124-139
[8]   Computer simulation of a biomass gasification-solid oxide fuel cell power system using Aspen Plus [J].
Doherty, Wayne ;
Reynolds, Anthony ;
Kennedy, David .
ENERGY, 2010, 35 (12) :4545-4555
[9]   Study on coal-fired power plant with CO2 capture by integrating Molten carbonate fuel cell system [J].
Duan, Liqiang ;
Xia, Kun ;
Feng, Tao ;
Jia, Shilun ;
Bian, Jing .
ENERGY, 2016, 117 :578-589
[10]   Study on a new IGCC (Integrated Gasification Combined Cycle) system with CO2 capture by integrating MCFC (Molten Carbonate Fuel Cell) [J].
Duan, Liqiang ;
Sun, Siyu ;
Yue, Long ;
Qu, Wanjun ;
Yang, Yongping .
ENERGY, 2015, 87 :490-503