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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

邮发代号 80-969

2019 Impact Factor: 3.552

Frontiers of Chemical Science and Engineering  2020, Vol. 14 Issue (4): 614-628   https://doi.org/10.1007/s11705-019-1849-5
  本期目录
An efficient technique for improving methanol yield using dual CO2 feeds and dry methane reforming
Yang Su1, Liping Lü2, Weifeng Shen1(), Shun’an Wei1
1. School of Chemistry and Chemical Engineering, Chongqing University, Chongqing 400044, China
2. School of Chemistry and Chemical Engineering, Yangtze Normal University, Chongqing 408100, China
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Abstract

Steam methane reforming (SMR)-based methanol synthesis plants utilizing a single CO2 feed represent one of the predominant technologies for improving methanol yield and CO2 utilization. However, SMR alone cannot achieve full CO2 utilization, and a high water content accumulates if CO2 is only fed into the methanol reactor. In this study, a process integrating SMR with dry methane reforming to improve the conversion of both methane and CO2 is proposed. We also propose an innovative methanol production approach in which captured CO2 is introduced into both the SMR process and the recycle gas of the methanol synthesis loop. This dual CO2 feed approach aims to optimize the stoichiometric ratio of the reactants. Comparative evaluations are carried out from a techno-economic point of view, and the proposed process is demonstrated to be more efficient in terms of both methanol productivity and CO2 utilization than the existing stand-alone natural gas-based methanol process.

Key wordsmethanol synthesis    CO2 utilization    dry methane reforming    steam methane reforming    process design
收稿日期: 2019-01-06      出版日期: 2020-05-22
Corresponding Author(s): Weifeng Shen   
 引用本文:   
. [J]. Frontiers of Chemical Science and Engineering, 2020, 14(4): 614-628.
Yang Su, Liping Lü, Weifeng Shen, Shun’an Wei. An efficient technique for improving methanol yield using dual CO2 feeds and dry methane reforming. Front. Chem. Sci. Eng., 2020, 14(4): 614-628.
 链接本文:  
https://academic.hep.com.cn/fcse/CN/10.1007/s11705-019-1849-5
https://academic.hep.com.cn/fcse/CN/Y2020/V14/I4/614
Fig.1  
Fig.2  
Fig.3  
Parameter Value
Particle density 1935 kgcat/m3cat
Particle diameter 5.5 mm
Fixed bed porosity 0.38
Tab.1  
k=A exp(BRT) A B
k1 ?29.87 4811.2
k2 8.147 0
k3 ?6.452 2068.4
k4 ?34.95 14928.9
k5 4804 ?11797.5
k6 17.55 ?2249.8
k7 0.1310 ?7023.5
Tab.2  
Fig.4  
Fig.5  
Component Proposed process Reference process
In /(t·h?1) Out /(t·h?1) In /(t·h?1) Out /(t·h?1)
CH4 28.49 1.24 28.49 4.98
CO2 28.96 5.08 20.63 4.81
CO 0 0.13 0 0.46
H2 0 0.083 0 0.84
H2O 82.87 62.29 82.87 62.94
Methanol 0 72.06 0 57.96
AR 0 0 0 0
N2 0.12 0.12 0.12 0.12
Total 140.44 140.44 132.11 132.11
Tab.3  
Fig.6  
Fig.7  
Fig.8  
Fig.9  
Fig.10  
Fig.11  
Fig.12  
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