Optimization for hydrogen production from methanol partial oxidation over NieCu/Al2O3 catalyst under sprays

被引:15
作者
Chih, Yi-Kai [1 ]
Su, Yu-Qi [1 ]
Chen, Wei-Hsin [1 ,2 ,3 ]
Lin, Bo-Jhih [1 ]
Kuo, Jenn-Kun [4 ]
You, Siming [5 ]
Lin, Hong-Ping [6 ]
机构
[1] Natl Cheng Kung Univ, Dept Aeronaut & Astronaut, Tainan 701, Taiwan
[2] Tunghai Univ, Res Ctr Smart Sustainable Circular Econ, Taichung 407, Taiwan
[3] Natl Chin Yi Univ Technol, Dept Mech Engn, Taichung 411, Taiwan
[4] Natl Univ Tainan, Dept Greenergy, Tainan 700, Taiwan
[5] Univ Glasgow, James Watt Sch Engn, Glasgow G12 8QQ, Lanark, Scotland
[6] Natl Cheng Kung Univ, Dept Chem, Tainan 701, Taiwan
关键词
Hydrogen production optimization; Partial oxidation of methanol (POM); Ni-Cu/Al2O3; catalyst; Sprays; Water gas shift reaction (WGSR); Response surface methodology (RSM); FUEL-CELL; HIGH-PERFORMANCE; OIL PRODUCTION; CU; DEHYDROGENATION; PARAMETERS; STORAGE; NICKEL; CO; PD;
D O I
10.1016/j.ijhydene.2021.06.103
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
In this work, a novel NieCu/Al2O3 catalyst is used to trigger the partial oxidation of methanol (POM) for hydrogen production. This reaction system also employed ultrasonic sprays to aid in dispersing methanol fuel. The prepared catalyst is analyzed by scanning electron microscope (SEM), energy-dispersive X-ray (EDX) spectroscopy, and X-ray diffraction (XRD) to explore the catalyst's surface structure, elemental composition, and physical structure, respectively. The Box-Behnken design (BBD) of response surface methodology (RSM) is utilized for experimental design to achieve process optimization. The operating parameters comprise the O-2/C molar ratio (0.5-0.7), preheating temperature (150-250 degrees C), and weight percent (wt%) of Ni (10-30%) in the catalyst. The results show that methanol conversion is 100% in all the operating conditions, while the reaction temperature for H-2 production ranges from 160 to 750 degrees C, stemming from heat released by POM. The significance and suitability of operating conditions are also analyzed by analysis of variance (ANOVA). It indicates that the highest H-2 yield is 2 mol (mol CH3OH)(-1), occurring at O-2/C = 0.5, preheating temperature = 150 degrees C, and Ni wt% = 10. Compared with the commercial h-BN-Pt/Al2O3 catalyst, the prepared NieCu/Al2O3 catalysts have higher activity for H-2 production. The O-2/C ratio is the most influential factor in the H-2 yield. Moreover, the
引用
收藏
页码:40559 / 40572
页数:14
相关论文
共 50 条
  • [31] Production of Hydrogen and Nanocarbon from Catalytic Decomposition of Methane over a Ni-Fe/Al2O3 Catalyst
    Wang, Gaowei
    Jin, Yi
    Liu, Guojuan
    Li, Yongdan
    [J]. ENERGY & FUELS, 2013, 27 (08) : 4448 - 4456
  • [32] Hydrogen and carbon nanofibers synthesis by methane decomposition over Ni-Pd/Al2O3 catalyst
    Bayat, Nima
    Rezaei, Mehran
    Meshkani, Fereshteh
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (12) : 5494 - 5503
  • [33] Kinetic modeling of steam reforming of ethanol for the production of hydrogen over Co/Al2O3 catalyst
    Sahoo, D. R.
    Vajpai, Shilpi
    Patel, Sanjay
    Pant, K. K.
    [J]. CHEMICAL ENGINEERING JOURNAL, 2007, 125 (03) : 139 - 147
  • [34] Partial oxidation of methane to synthesize gas over Ni/α-Al2O3 catalyst promoted by noble metals
    Yan, QG
    Yu, ZL
    Yuan, SY
    [J]. CHEMICAL JOURNAL OF CHINESE UNIVERSITIES-CHINESE, 1998, 19 (04): : 626 - 628
  • [35] Hydrogen production from low-temperature methanol steam reforming over silver-promoted CuO/ZnO/Ag/Al2O3 Catalyst
    Zhang, Saibei
    Qu, Xiaohan
    Lv, Hui
    Mao, Jingbo
    Zhou, Jinxia
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2024, 77 : 1317 - 1326
  • [36] Degreening Effect During NO Oxidation over Pt/Al2O3 Catalyst
    Jia Liwei
    Wan Taoming
    Wang Jun
    Shen Meiqing
    Wang Jianqiang
    Wang Jiaming
    [J]. RARE METAL MATERIALS AND ENGINEERING, 2018, 47 (05) : 1562 - 1566
  • [37] Catalytic dehydration of methanol to dimethyl ether over modified γ-Al2O3 catalyst
    Liu, Dianhua
    Yao, Chunfeng
    Zhang, Jianqiang
    Fang, Dingye
    Chen, Dasheng
    [J]. FUEL, 2011, 90 (05) : 1738 - 1742
  • [38] Hydrogen production from wood vinegar of camellia oleifera shell by Ni/M/γ-Al2O3 catalyst
    Xu, Xiwei
    Jiang, Enchen
    Li, Bosong
    Wang, Mingfeng
    Wang, Gang
    Ma, Qian
    Shi, Dongdong
    Guo, Xinhui
    [J]. CATALYSIS COMMUNICATIONS, 2013, 39 : 106 - 114
  • [39] SOFT MECHANOCHEMICAL SYNTHESIS OF CuO/ZnO/AL2O3 CATALYST FOR METHANOL PRODUCTION
    Kournikova, A. A.
    Rumyantsev, R. N.
    Afineevsky, A. V.
    Borisova, T. N.
    Severgina, E. S.
    Gordina, N. E.
    [J]. IZVESTIYA VYSSHIKH UCHEBNYKH ZAVEDENII KHIMIYA I KHIMICHESKAYA TEKHNOLOGIYA, 2024, 67 (02): : 21 - 29
  • [40] Kinetics of Hydrogen and Toluene Production from Methylcyclohexane in the Presence of a PtSn/Al2O3 Catalyst
    Lozhkin, A. D.
    Iskhakova, L. D.
    Milovich, F. O.
    Katsman, E. A.
    Bruk, L. G.
    [J]. KINETICS AND CATALYSIS, 2024, 65 (03) : 280 - 297