Knowledge Management System Of Guangzhou Institute of Energy Conversion, CAS
Study on methane hydration process in a semi-continuous stirred tank reactor | |
Hao, Wenfeng; Wang, Jinqu; Fan, Shuanshi; Hao, Wenbin | |
2007-03-01 | |
Source Publication | ENERGY CONVERSION AND MANAGEMENT |
ISSN | 0196-8904 |
Volume | 48Issue:3Pages:954-960 |
Corresponding Author | haowenfeng@163.com |
Abstract | The methane hydration process is investigated in a semi-continuous stirred tank reactor. Liquid temperatures and reaction rates without stirrer are compared with those occurring with stirrer, while at the same time better stirring conditions of the methane hydration process are given by the experiments. Some basic data of fluid mechanics, for example, stirring Reynolds number, Froucle number and stirrer power, are calculated during the methane hydration process, which can be applied to evaluate stirrer capacity and provide some basic data for a scaled up reactor. Based on experiment and calculations in this work, some conclusions are drawn. First, the stirrer has great influence on the methane hydration process. Batch stirring is helpful to improve the mass transfer and heat transfer performances of the methane hydration process. Second, induction time can be shortened effectively by use of the stirrer. Third, in this paper, the appropriate stirring velocity and stirring time were 320 rpm and 30 min, respectively, at 5.0 MPa, for which the storage capacity and reaction time were 159.1 V/V and 370 min, respectively. Under the condition of the on-flow state, the initial stirring Reynolds number of the fluid and the stirring power were 12,150 and 0.54 W, respectively. Fourth, some suggestions, for example, the use of another type of stirrer or some baffles, are proposed to accelerate the methane hydration process. Comparing with literature data, higher storage capacity and hydration rate are achieved in this work. Moreover, some fluid mechanics parameters are calculated, which can provide some references to engineering application. (c) 2006 Elsevier Ltd. All rights reserved. |
Subtype | Article |
Other Abstract | The methane hydration process is investigated in a semi-continuous stirred tank reactor. Liquid temperatures and reaction rates without stirrer are compared with those occurring with stirrer, while at the same time better stirring conditions of the methane hydration process are given by the experiments. Some basic data of fluid mechanics, for example, stirring Reynolds number, Froucle number and stirrer power, are calculated during the methane hydration process, which can be applied to evaluate stirrer capacity and provide some basic data for a scaled up reactor. Based on experiment and calculations in this work, some conclusions are drawn. First, the stirrer has great influence on the methane hydration process. Batch stirring is helpful to improve the mass transfer and heat transfer performances of the methane hydration process. Second, induction time can be shortened effectively by use of the stirrer. Third, in this paper, the appropriate stirring velocity and stirring time were 320 rpm and 30 min, respectively, at 5.0 MPa, for which the storage capacity and reaction time were 159.1 V/V and 370 min, respectively. Under the condition of the on-flow state, the initial stirring Reynolds number of the fluid and the stirring power were 12,150 and 0.54 W, respectively. Fourth, some suggestions, for example, the use of another type of stirrer or some baffles, are proposed to accelerate the methane hydration process. Comparing with literature data, higher storage capacity and hydration rate are achieved in this work. Moreover, some fluid mechanics parameters are calculated, which can provide some references to engineering application. |
Keyword | Methane Hydration Process Semi-continuous Stirred Tank Reactor Stirring Reynolds Number Froude Number Stirrer Power Storage Capacity Hydration Rate |
WOS Headings | Science & Technology ; Physical Sciences ; Technology |
DOI | 10.1016/j.enconman.2006.08.007 |
WOS Subject Extended | Thermodynamics ; Energy & Fuels ; Mechanics ; Physics |
URL | 查看原文 |
WOS Keyword | GAS HYDRATE ; STORAGE ; SURFACTANTS |
Indexed By | SCI |
Language | 英语 |
WOS Subject | Thermodynamics ; Energy & Fuels ; Mechanics ; Physics, Nuclear |
WOS ID | WOS:000244495000031 |
Citation statistics | |
Document Type | 期刊论文 |
Identifier | http://ir.giec.ac.cn/handle/344007/3500 |
Collection | 中国科学院广州能源研究所 |
Affiliation | 1.Dalian Univ Technol, State Key Lab Fine Chem, Inst Adsorpt & Inorgan Membrane, Dalian 116012, Liaoning, Peoples R China 2.Chinese Acad Sci, Guangzhou Inst Energy Convers, Ctr Nat Gas Hydrate Res, Guangzhou 510640, Guangdong, Peoples R China 3.SW Jiaotong Univ, Sch Elect Engn, Chengdu 610031, Sichuan, Peoples R China |
Recommended Citation GB/T 7714 | Hao, Wenfeng,Wang, Jinqu,Fan, Shuanshi,et al. Study on methane hydration process in a semi-continuous stirred tank reactor[J]. ENERGY CONVERSION AND MANAGEMENT,2007,48(3):954-960. |
APA | Hao, Wenfeng,Wang, Jinqu,Fan, Shuanshi,&Hao, Wenbin.(2007).Study on methane hydration process in a semi-continuous stirred tank reactor.ENERGY CONVERSION AND MANAGEMENT,48(3),954-960. |
MLA | Hao, Wenfeng,et al."Study on methane hydration process in a semi-continuous stirred tank reactor".ENERGY CONVERSION AND MANAGEMENT 48.3(2007):954-960. |
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