Performance enhancement of a plate methanol steam reformer by ribs installed in the reformer channel

被引:15
作者
Perng, Shiang-Wuu [1 ]
Chien, Tsai-Chieh [1 ]
Horng, Rong-Fang [1 ]
Wu, Horng-Wen [2 ]
机构
[1] Kun Shan Univ, Dept Mech Engn, 195 Kunda Rd, Tainan 710, Taiwan
[2] Natl Cheng Kung Univ, Dept Syst & Naval Mechatron Engn, Tainan 710, Taiwan
关键词
Plate methanol steam reformer; Transverse rib; Hydrogen yield; Estimated cell net power of PEMFC; PACKED-BED REACTORS; MEMBRANE FUEL-CELL; HYDROGEN-PRODUCTION; REACTANT TRANSPORT; MICRO-REFORMER; FLOW; CATALYST; DESIGN; GENERATION; GEOMETRY;
D O I
10.1016/j.energy.2018.10.176
中图分类号
O414.1 [热力学];
学科分类号
摘要
The plate methanol steam reformer (PMSR) designed to enhance its performance is connected with proton exchange membrane fuel cells (PEMFC) considered as a bright future power source. The influences of height and width of transverse ribs, and heating temperature of PMSR were investigated on thermal flow fields, hydrogen yield, methanol conversion, and estimated cell net power of PEMFC. The outcomes show that only heating temperature of 250 degrees C can meet this requirement that the CO concentration lower than 10 ppm can sustain PEMFC operation, so the effect of transverse rib height and width is discussed at heating temperature of 250 degrees C. Compared to the traditional PMSR, a PMSR with the transverse ribs of 1.5 mm height and 4 mm width improves the conversion of methanol up to 19.58% and the hydrogen yield up to 57.23%. The PMSR installing the transverse ribs with 1.125 mm height and 4 mm width enhances the estimated cell net power output of a PEMFC up to 14.20%. The ribs installed in the reformer channel can effectively enhances the conversion of methanol and hydrogen yield of a PMSR and the estimated cell net power output of a PEMFC compared with the traditional PMSR. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:588 / 601
页数:14
相关论文
共 39 条
  • [1] Steam reforming of methanol over a Cu/ZnO/Al2O3 catalyst:: a kinetic analysis and strategies for suppression of CO formation
    Agrell, J
    Birgersson, H
    Boutonnet, M
    [J]. JOURNAL OF POWER SOURCES, 2002, 106 (1-2) : 249 - 257
  • [2] An investigation into the effect of manifold geometry on uniformity of temperature distribution in a PEMFC stack
    Amirfazli, Amir
    Asghari, Saeed
    Sarraf, Mohammad
    [J]. ENERGY, 2018, 145 : 141 - 151
  • [3] Bejan A, 1995, CONVECTION HEAT TRAN, P525
  • [4] Numerical study on a novel 3D cathode flow field and evaluation criteria for the PEM fuel cell design
    Cai, Yonghua
    Fang, Zhou
    Chen, Ben
    Yang, Tianqi
    Tu, Zhengkai
    [J]. ENERGY, 2018, 161 : 28 - 37
  • [5] Thermal resistance effect on methanol-steam reforming performance in micro-scale reformers
    Chein, Rei-Yu
    Chen, Yen-Cho
    Chung, J. N.
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (01) : 250 - 262
  • [6] Hydrogen production using integrated methanol-steam reforming reactor with various reformer designs for PEM fuel cells
    Chein, Rei-Yu
    Chen, Yen-Cho
    Lin, Yu-Sheng
    Chung, J. N.
    [J]. INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2012, 36 (04) : 466 - 476
  • [7] CFD (computational fluid dynamics)-based optimal design of a micro-reformer by integrating computational a fluid dynamics code using a simplified conjugate-gradient method
    Cheng, Chin-Hsiang
    Huang, Yu-Xian
    King, Shun-Chih
    Lee, Chun-I
    Leu, Chih-Hsing
    [J]. ENERGY, 2014, 70 : 355 - 365
  • [8] A review of PEM hydrogen fuel cell contamination: Impacts, mechanisms, and mitigation
    Cheng, Xuan
    Shi, Zheng
    Glass, Nancy
    Zhang, Lu
    Zhang, Jiujun
    Song, Datong
    Liu, Zhong-Sheng
    Wang, Haijiang
    Shen, Jun
    [J]. JOURNAL OF POWER SOURCES, 2007, 165 (02) : 739 - 756
  • [9] ERGUN S, 1952, CHEM ENG PROG, V48, P89
  • [10] Review of developments in portable hydrogen production using microreactor technology
    Holladay, JD
    Wang, Y
    Jones, E
    [J]. CHEMICAL REVIEWS, 2004, 104 (10) : 4767 - 4789