Compact Heat Integrated Reactor System of Steam Reformer, Shift Reactor and Combustor for Hydrogen Production from Ethanol

被引:5
|
作者
Khaodee, Watcharapong [1 ,2 ]
Jiwanuruk, Tara [3 ]
Ountaksinkul, Khunnawat [3 ]
Charojrochkul, Sumittra [4 ]
Charoensuk, Jarruwat [5 ]
Wongsakulphasatch, Suwimol [6 ]
Assabumrungrat, Suttichai [3 ]
机构
[1] Mahanakorn Univ Technol, Dept Chem Engn, Bangkok 10530, Thailand
[2] Naresuan Univ, Fac Engn, Dept Ind Engn, Chem Engn Program, Phitsanulok 65000, Thailand
[3] Chulalongkorn Univ, Fac Engn, Ctr Excellence Catalysis & Catalyt React Engn, Dept Chem Engn, Bangkok 10330, Thailand
[4] Natl Met & Mat Technol Ctr MTEC, Pathum Thani 12120, Thailand
[5] King Mongkuts Inst Technol Ladkrabang, Fac Engn, Mech Engn Dept, Bangkok 10520, Thailand
[6] King Mongkuts Univ Technol North Bangkok, Fac Engn, Dept Chem Engn, Bangkok 10800, Thailand
关键词
compact reactor; ethanol steam reforming; water gas shift; hydrogen production; WATER-GAS SHIFT; THERMODYNAMIC ANALYSIS; BIO-OIL; FUEL; CATALYSTS; MICROREACTORS; SIMULATION; OXIDATION;
D O I
10.3390/pr8060708
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A compact heat integrated reactor system (CHIRS) of a steam reformer, a water gas shift reactor, and a combustor were designed for stationary hydrogen production from ethanol. Different reactor integration concepts were firstly studied using Aspen Plus. The sequential steam reformer and shift reactor (SRSR) was considered as a conventional system. The efficiency of the SRSR could be improved by more than 12% by splitting water addition to the shift reactor (SRSR-WS). Two compact heat integrated reactor systems (CHIRS) were proposed and simulated by using COMSOL Multiphysics software. Although the overall efficiency of the CHIRS was quite a bit lower than the SRSR-WS, the compact systems were properly designed for portable use. CHIRS (I) design, combining the reactors in a radial direction, was large in reactor volume and provided poor temperature control. As a result, the ethanol steam reforming and water gas shift reactions were suppressed, leading to lower hydrogen selectivity. On the other hand, CHIRS (II) design, combining the process in a vertical direction, provided better temperature control. The reactions performed efficiently, resulting in higher hydrogen selectivity. Therefore, the high performance CHIRS (II) design is recommended as a suitable stationary system for hydrogen production from ethanol.
引用
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页数:19
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