Carbon dioxide hydrate separation from Integrated Gasification Combined Cycle (IGCC) syngas by a novel hydrate heat-mass coupling method
文献类型：期刊论文
| 作者 | Chen, Zhaoyang2,3,4; Fang, Jie1,3,4; Xu, Chungang2,3,4; Xia, Zhiming2,3,4; Yan, Kefeng2,3,4 ; Li, Xiaosen2,3,4
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| 刊名 | ENERGY
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| 出版日期 | 2020-05-15 |
| 卷号 | 199页码:12 |
| 关键词 | CO2 hydrate separation Bubbling reaction IGCC Heat-mass coupling TBAB hydrate |
| ISSN号 | 0360-5442 |
| DOI | 10.1016/j.energy.2020.117420 |
| 通讯作者 | Li, Xiaosen(lixs@ms.giec.ac.cn) |
| 英文摘要 | 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. |
| WOS关键词 | PRE-COMBUSTION CAPTURE ; SIMULATED FUEL GAS ; CO2 CAPTURE ; NATURAL-GAS ; CLATHRATE HYDRATE ; PHASE-EQUILIBRIUM ; HBGS PROCESS ; LATENT-HEAT ; FLUE-GAS ; TBAB |
| 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 |
| 语种 | 英语 |
| WOS记录号 | WOS:000527571300068 |
| 出版者 | PERGAMON-ELSEVIER SCIENCE LTD |
| 资助机构 | National Natural Science Foundation of China ; Special Project for Marine Economy Development of Guangdong Province ; CAS Science and Technology Apparatus Development Program |
| 源URL | [http://ir.giec.ac.cn/handle/344007/26706]  |
| 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.Univ Sci & Technol China, Nano Sci & Technol Inst, Suzhou 215123, Jiangsu, Peoples R China 2.Guangdong Key Lab New & Renewable Energy Res & De, Guangzhou 510640, Peoples R China 3.CAS Key Lab Gas Hydrate, Guangzhou 510640, Peoples R China 4.Chinese Acad Sci, Guangzhou Ctr Gas Hydrate Res, Guangzhou Inst Energy Convers, Guangzhou 510640, 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. |
入库方式： OAI收割
来源：广州能源研究所
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