Study of the coke distribution in MTO fluidized bed reactor with MP-PIC approach
文献类型:期刊论文
作者 | Ye, Mao2; Yuan, Xiaoshuai1,2; Li, Hua2; Liu, Zhongmin2 |
刊名 | CANADIAN JOURNAL OF CHEMICAL ENGINEERING
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出版日期 | 2019-02-01 |
卷号 | 97期号:2页码:500-510 |
关键词 | MTO Coke distribution fluidized bed CFD MP-PIC |
ISSN号 | 0008-4034 |
DOI | 10.1002/cjce.23239 |
通讯作者 | Ye, Mao(maoye@dicp.ac.cn) |
英文摘要 | The methanol to olefins (MTO) process has received considerable interest due to its importance in transforming abundant resources such as coal, natural gas, and biomass to widely-demanded light olefins. In the MTO process, the coke deposited on the catalyst governs the catalyst activity and product selectivity, and thus is critical to the reaction behaviour. In the industrial processes, the residence time and coke content of catalyst particles in the reactor show a certain distribution due to the continuous outflow of spent catalyst and inflow of regenerated catalyst, which need further attention. The multi-phase particle-in-cell (MP-PIC) approach was used in the current work to simulate the catalyst residence time and coke content distribution. The effect of gas-solid flow patterns, reactor structure, and average catalyst residence time on the residence time and coke content distribution was investigated. It was found that at high superficial velocities, the coke content distributions obtained with the MP-PIC method are consistent with the distribution deduced from the ideally mixed flow assumption of catalyst particles. The results suggested that it is possible to simulate large-scale MTO reactors by use of the coke distribution. In particular, by incorporating an initial coke distribution, the time needed to reach steady state in the MTO reactor simulations could be greatly reduced. |
WOS关键词 | DISCRETE PARTICLE SIMULATION ; IN-CELL MODEL ; NUMERICAL-SIMULATION ; PROPYLENE PROCESS ; FILTERED MODEL ; METHANOL ; OLEFINS ; FLOW ; CONVERSION ; OPTIMIZATION |
资助项目 | National Natural Science Foundation of China[91334205] |
WOS研究方向 | Engineering |
语种 | 英语 |
WOS记录号 | WOS:000455520100009 |
出版者 | WILEY |
资助机构 | National Natural Science Foundation of China ; National Natural Science Foundation of China ; National Natural Science Foundation of China ; National Natural Science Foundation of China ; National Natural Science Foundation of China ; National Natural Science Foundation of China ; National Natural Science Foundation of China ; National Natural Science Foundation of China |
源URL | [http://cas-ir.dicp.ac.cn/handle/321008/166208] ![]() |
专题 | 大连化学物理研究所_中国科学院大连化学物理研究所 |
通讯作者 | Ye, Mao |
作者单位 | 1.Univ Chinese Acad Sci, Beijing 100049, Peoples R China 2.Chinese Acad Sci, Dalian Inst Chem Phys, Natl Engn Lab MTO, Dalian Natl Lab Clean Energy, Dalian 116023, Peoples R China |
推荐引用方式 GB/T 7714 | Ye, Mao,Yuan, Xiaoshuai,Li, Hua,et al. Study of the coke distribution in MTO fluidized bed reactor with MP-PIC approach[J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING,2019,97(2):500-510. |
APA | Ye, Mao,Yuan, Xiaoshuai,Li, Hua,&Liu, Zhongmin.(2019).Study of the coke distribution in MTO fluidized bed reactor with MP-PIC approach.CANADIAN JOURNAL OF CHEMICAL ENGINEERING,97(2),500-510. |
MLA | Ye, Mao,et al."Study of the coke distribution in MTO fluidized bed reactor with MP-PIC approach".CANADIAN JOURNAL OF CHEMICAL ENGINEERING 97.2(2019):500-510. |
入库方式: OAI收割
来源:大连化学物理研究所
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