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
收藏
页数:19
相关论文
共 50 条
  • [21] Catalytic reformer-combustor: A novel reactor concept for synthesis gas production
    Mleczko, L.
    Malcus, S.
    Wurzel, T.
    Industrial and Engineering Chemistry Research, 1997, 36 (11): : 4459 - 4465
  • [22] A Computational Investigation of Hydrogen Production from Methane Steam Reactor
    Panagakos, Grigorios
    Kyriakides, Alexios-Spyridon
    Papadopoulou, Simira
    Voutetakis, Spyros
    PRES15: PROCESS INTEGRATION, MODELLING AND OPTIMISATION FOR ENERGY SAVING AND POLLUTION REDUCTION, 2015, 45 : 1033 - 1038
  • [23] Initial study on steam reformer of high-temperature gas-cooled reactor powered steam methane reforming hydrogen production system
    Advanced Reactor Engineering and Safety Key Laboratory, Institute of Nuclear and New Energy Technology, Tsinghua University, Beijing 100084, China
    Yuanzineng Kexue Jishu, 2006, 4 (406-410):
  • [24] ANOVA analysis of an integrated membrane reactor for hydrogen production by methane steam reforming
    Leonzio, Grazia
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2019, 44 (23) : 11535 - 11545
  • [25] An experimental study on the reaction characteristics of a coupled reactor with a catalytic combustor and a steam reformer for SOFC systems
    Ghang, T. G.
    Lee, S. M.
    Ahn, K. Y.
    Kim, Y.
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (04) : 3234 - 3241
  • [26] Hydrogen production from bio-ethanol steam reforming reaction in a Pd/PSS membrane reactor
    Seelam, Prem K.
    Liguori, Simona
    Iulianelli, Adolfo
    Pinacci, Pietro
    Calabro, Vincenza
    Huuhtanen, Mika
    Keiski, Riitta
    Piemonte, Vincenzo
    Tosti, Silvano
    De Falco, Marcello
    Basile, Angelo
    CATALYSIS TODAY, 2012, 193 (01) : 42 - 48
  • [27] A numerical investigation of hydrogen production in an integrated membrane reformer-combustor
    Sanusi, Yinka S.
    Mokheimer, Esmail M. A.
    PROCEEDINGS OF THE 9TH INTERNATIONAL CONFERENCE ON APPLIED ENERGY, 2017, 142 : 1077 - 1082
  • [28] Performance analysis of a membrane-based reformer-combustor reactor for hydrogen generation
    Sanusi, Yinka S.
    Mokheimer, Esmail M. A.
    INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2019, 43 (01) : 189 - 203
  • [29] Hydrogen production by ethanol steam reforming: Experimental study of a Pd-Ag membrane reactor and traditional reactor behaviour
    Basile, Angelo
    Gallucci, Fausto
    Iulianelli, Adolfo
    De Falco, Marcello
    Liguori, Simona
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2008, 6
  • [30] A compact and high-efficiency electrified reactor for hydrogen production by methane steam reforming
    Ma, Jing
    Jiang, Bo
    Gao, Yuming
    Yu, Kewei
    Lv, Zheng
    Si-ma, Wang
    Yuan, Dazhong
    Tang, Dawei
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2022, 47 (98) : 41421 - 41431