DOI: 10.1016/j.jcou.2013.11.002
Scopus记录号: 2-s2.0-84890534061
论文题名: Simulation of fluidized bed reactor for producing synthesis gas by catalytic CH4-CO2 reforming
作者: Agrawal V. ; Srivastava V.C.
刊名: Journal of CO2 Utilization
ISSN: 22129820
出版年: 2014
卷: 5 起始页码: 10
结束页码: 16
语种: 英语
英文关键词: CO2 reforming of methane
; Dry reforming of methane
; Fluidized bed reactor
; Generalized comprehensive reactor model
; Syn-gas
Scopus关键词: Dry reforming-of-methane
; Fluidized bed reactors
; Reactor modeling
; Reforming of methane
; Syn-gas
; Carbon dioxide
; Catalysts
; Catalytic reforming
; Chemical reactors
; Fluid catalytic cracking
; Fluidized bed furnaces
; Methane
; Productivity
; Synthesis gas
; Loading
英文摘要: Catalytic CH4-CO2 reforming combines methane and CO2 to produce synthesis gas. In the present paper, dry reforming of methane has been simulated in a fluidized bed reactor using a modified comprehensive reactor model. The model has been employed to study the effect of various operating parameters like CO2CH4 feed ratio, gas hourly space velocity (GHSV), pressure (P) and catalyst loading (w) on CH 4 conversion (XCH4), CO + H2 productivity and CO/H2 molar ratio in product. Simulation results were compared with experimental data reported in the literature (Chem. Eng. Sci. 2000, 55, 3955-3966). At the optimum condition (CO2/CH4 molar ratio = 1.5, temperature = 1073 K, GHSV = 1100 h-1, pressure = 0.1 MPa and catalyst loading (w) = 120 g), values of XCH4, CO + H2 productivity and CO/H2 molar ratio in product were found to be 97.64%, 2.41 and 1.26, respectively. © 2013 Elsevier Ltd. All rights reserved. Citation statistics:
资源类型: 期刊论文
标识符: http://119.78.100.158/handle/2HF3EXSE/53001
Appears in Collections: 影响、适应和脆弱性
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Recommended Citation:
Agrawal V.,Srivastava V.C.. Simulation of fluidized bed reactor for producing synthesis gas by catalytic CH4-CO2 reforming[J]. Journal of CO2 Utilization,2014-01-01,5