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Carbon dioxide hydrate separation from Integrated Gasification Combined Cycle (IGCC) syngas by a novel hydrate heat-mass coupling method
Chen, Zhaoyang1,2,3; Fang, Jie1,2,4; Xu, Chungang1,2,3; Xia, Zhiming1,2,3; Yan, Kefeng1,2,3; Li, Xiaosen1,2,3
2020-05-15
发表期刊ENERGY
ISSN0360-5442
卷号199页码:12
通讯作者Li, Xiaosen(lixs@ms.giec.ac.cn)
摘要A novel hydrate heat-mass coupling separation (HHMCS) method was studied to reduce the energy consumption of CO2 hydrate separation from Integrated Gasification Combined Cycle (IGCC) syngas in this work. Tetra-n-butyl ammonium bromide (TBAB) is used as a hydrate promoter and pure TBAB hydrate is used as a phase change heat-mass coupling additive. The heat-mass coupling effect, CO2 separation characteristics and influence factors were studied by continuous separation experiments in a bubble column reactor. Compared to conventional gas hydrate separation method, the HHMCS process exhibits a higher energy-saving potential, less temperature and TBAB concentration fluctuation due to pure TBAB hydrate phase change. Increase inlet gas rate, the accumulated gas consumption decreased slightly, but the average gas consumption rate increased. Increase operating pressure and decrease gas phase volume increased the average gas consumption rate and CO2 separation efficiency. After continuous separation of simulated syngas, the average CO2 concentration in H-2-rich gas decreased to 17.45 mol %, and that in CO2-rich gas increased to 86.44 mol%. The CO2 split fraction and separation factor reached 0.80 and 8.15, respectively. The work provided a new idea to integrally utilize the phase change enthalpy, improve the operating flexibility and heat transfer in large device. (C) 2020 Elsevier Ltd. All reserved.
关键词CO2 hydrate separation Bubbling reaction IGCC Heat-mass coupling TBAB hydrate
DOI10.1016/j.energy.2020.117420
关键词[WOS]PRE-COMBUSTION CAPTURE ; SIMULATED FUEL GAS ; CO2 CAPTURE ; NATURAL-GAS ; CLATHRATE HYDRATE ; PHASE-EQUILIBRIUM ; HBGS PROCESS ; LATENT-HEAT ; FLUE-GAS ; TBAB
收录类别SCI
语种英语
资助项目National Natural Science Foundation of China[51576202] ; National Natural Science Foundation of China[51736009] ; Special Project for Marine Economy Development of Guangdong Province[GDME-2018D002] ; CAS Science and Technology Apparatus Development Program[YZ201619]
WOS研究方向Thermodynamics ; Energy & Fuels
项目资助者National Natural Science Foundation of China ; Special Project for Marine Economy Development of Guangdong Province ; CAS Science and Technology Apparatus Development Program
WOS类目Thermodynamics ; Energy & Fuels
WOS记录号WOS:000527571300068
出版者PERGAMON-ELSEVIER SCIENCE LTD
引用统计
被引频次:19[WOS]   [WOS记录]     [WOS相关记录]
文献类型期刊论文
条目标识符http://ir.giec.ac.cn/handle/344007/26707
专题中国科学院广州能源研究所
通讯作者Li, Xiaosen
作者单位1.Chinese Acad Sci, Guangzhou Ctr Gas Hydrate Res, Guangzhou Inst Energy Convers, Guangzhou 510640, Peoples R China
2.CAS Key Lab Gas Hydrate, Guangzhou 510640, Peoples R China
3.Guangdong Key Lab New & Renewable Energy Res & De, Guangzhou 510640, Peoples R China
4.Univ Sci & Technol China, Nano Sci & Technol Inst, Suzhou 215123, Jiangsu, Peoples R China
推荐引用方式
GB/T 7714
Chen, Zhaoyang,Fang, Jie,Xu, Chungang,et al. Carbon dioxide hydrate separation from Integrated Gasification Combined Cycle (IGCC) syngas by a novel hydrate heat-mass coupling method[J]. ENERGY,2020,199:12.
APA Chen, Zhaoyang,Fang, Jie,Xu, Chungang,Xia, Zhiming,Yan, Kefeng,&Li, Xiaosen.(2020).Carbon dioxide hydrate separation from Integrated Gasification Combined Cycle (IGCC) syngas by a novel hydrate heat-mass coupling method.ENERGY,199,12.
MLA Chen, Zhaoyang,et al."Carbon dioxide hydrate separation from Integrated Gasification Combined Cycle (IGCC) syngas by a novel hydrate heat-mass coupling method".ENERGY 199(2020):12.
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