Optimization of methanol steam reforming for hydrogen production

被引:0
|
作者
机构
[1] [1,Zhang, Lei
[2] Pan, Li-Wei
[3] Ni, Chang-Jun
[4] Zhao, Sheng-Sheng
[5] Wang, Shu-Dong
[6] Hu, Yong-Kang
[7] Wang, An-Jie
[8] Jiang, Kai
来源
Pan, L.-W. (panlw@dicp.ac.cn) | 2013年 / Science Press卷 / 41期
关键词
Central composite rotatable design - Central composite rotatable design CCRD) - CO concentrations - Full factorial design - Gas hourly space velocities - Methanol-steam reforming - Optimisations - Reaction temperature - Reformed gas - Response surface;
D O I
暂无
中图分类号
学科分类号
摘要
The catalytic performance of CuO/ZnO/CeO2/ZrO2 prepared by co-precipitation for methanol steam reforming was investigated using a statistical set of experiments in order to optimize the reaction conditions for obtaining minimal carbon monoxide in the reformed gas. The reaction temperature, steam to methanol ratio, methanol gas hourly space velocity (GHSV) were evaluated with a full factorial design experiment. The reaction temperature displayed much greater influence on the response (methanol conversion and CO concentration in reformed gas), GHSV has minimal influence on the CO concentration in reformed gas. At a fixed low methanol GHSV (300 h-1), a central composite rotatable design was then used to approximate the optimal conditions by simultaneously considering the methanol conversion and CO concentration. The optimum theoretical conditions were found to lie within a reaction temperature of 249~258°C and a W/M ratio of 1.76~2.00, in close agreement with the experimental results.
引用
收藏
相关论文
共 50 条
  • [1] Optimization analysis of methanol steam reforming for hydrogen production
    Wang, Feng
    Zheng, Shi-Wei
    Zhang, Ding-Wen
    Qi, Bo
    Zhang, Xiang-Yu
    Chongqing Daxue Xuebao/Journal of Chongqing University, 2009, 32 (12): : 1410 - 1413
  • [2] Hydrogen production by steam reforming of methanol
    Iwasa, N
    Nomura, W
    Mayanagi, T
    Fujita, S
    Arai, M
    Takezawa, N
    JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2004, 37 (02) : 286 - 293
  • [3] Methanol steam reforming for hydrogen production
    Palo, Daniel R.
    Dagle, Robert A.
    Holladay, Jamie D.
    CHEMICAL REVIEWS, 2007, 107 (10) : 3992 - 4021
  • [4] Simulations of Hydrogen Production by Methanol Steam Reforming
    Chiu, Yu-Jen
    Chiu, Han-Chieh
    Hsieh, Ren-Horn
    Jang, Jer-Huan
    Jiang, Bo-Yi
    5TH INTERNATIONAL CONFERENCE ON POWER AND ENERGY SYSTEMS ENGINEERING (CPESE 2018), 2019, 156 : 38 - 42
  • [5] Methanol steam reforming for hydrogen production in a minireactor
    Wang, Feng
    Li, Longjian
    Qi, Bo
    Cui, Wenzhi
    Xin, Mingdao
    Chen, Qinghua
    Deng, Lianfeng
    Hsi-An Chiao Tung Ta Hsueh/Journal of Xi'an Jiaotong University, 2008, 42 (04): : 509 - 514
  • [6] Intensification of hydrogen production by methanol steam reforming
    Sanz, Oihane
    Velasco, Ion
    Perez-Miqueo, Inigo
    Poyato, Rosalia
    Antonio Odriozola, Jose
    Montes, Mario
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (10) : 5250 - 5259
  • [7] Hydrogen Production by Methanol Steam Reforming Using Microreactor
    Kawamura, Yoshihiro
    Ogura, Naotsugu
    Igarashi, Akira
    JOURNAL OF THE JAPAN PETROLEUM INSTITUTE, 2013, 56 (05) : 288 - 297
  • [8] Nanosized catalysts for the production of hydrogen by methanol steam reforming
    Valdes-Solis, T.
    Marban, G.
    Fuertes, A. B.
    CATALYSIS TODAY, 2006, 116 (03) : 354 - 360
  • [9] Hydrogen production process based on methanol steam reforming
    Hao, Shuren
    Li, Yanhao
    Cheng, Yuchun
    Wang, Zhiliang
    Jingxi Huagong/Fine Chemicals, 1998, 15 (05): : 52 - 54
  • [10] Thermochemical Module for Hydrogen Production by Steam Reforming of Methanol
    A. V. Makunin
    M. S. Granovskii
    E. B. Ivanov
    V. M. Fomin
    Chemical and Petroleum Engineering, 2003, 39 : 704 - 710