Effect of impurities of CH3OH, CH3COOH, and KOH on aqueous phase reforming of glycerol over mesoporous Ni-Cu/CeO2 catalyst

被引:21
作者
Wu, Kai [1 ]
Dou, Binlin [1 ]
Zhang, Hua [1 ]
Liu, Dashuai [1 ]
Chen, Haisheng [2 ]
Xu, Yujie [2 ]
机构
[1] Univ Shanghai Sci & Technol, Shanghai Key Lab Multiphase Flow & Heat Transfer, Sch Energy & Power Engn, Shanghai 200093, Peoples R China
[2] Chinese Acad Sci, Inst Engn Thermophys, Beijing 100190, Peoples R China
关键词
Hydrogen production; Aqueous phase reforming; Mesoporous Ni-Cu/CeO2 catalyst; In-situ CO2 capture; COX-FREE HYDROGEN; WATER-GAS SHIFT; OXYGENATED HYDROCARBONS; POTASSIUM HYDROXIDE; RENEWABLE HYDROGEN; ACETIC-ACID; NI; METHANOL; CU; 1,2-PROPANEDIOL;
D O I
10.1016/j.joei.2021.09.009
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Impurities are inevitable in crude glycerol, a by-product of biodiesel, which has a great influence on aqueous phase reforming (APR). This work investigates three impurities (CH3OH, CH3COOH, and KOH) in the aqueous phase reforming of glycerol (GAPR) using a mesoporous Ni-Cu/CeO2 catalyst at three temperatures. The experiment results indicate that the increase of temperature is beneficial to the conversion of glycerol into gas products, but not favor to the proportion of H-2 in the gas phase. The presence of CH3OH almost has not affected the total gas volume, while CH3COOH and KOH decreased and increased the gas volume, respectively. The deactivation of the catalyst occurs under acidic conditions because the active phase Ni on the catalyst surface is lost in the hydrogen evolution reaction. KOH has the greatest influence on the gas phase composition, which greatly increases the H-2 production and the proportion of H-2. The results of liquid-phase solution analysis show that the addition of CH3COOH promoted the dehydration of glycerol, which is contrary to the results obtained by adding KOH. CH3OH, as the final product of glycerol dehydrogenation and decarbonization, is added to the initial solution, which will be conducive to the dehydration reaction. The addition of CaO can increase the H-2 production in the APR of glycerol solution containing impurities.
引用
收藏
页码:198 / 208
页数:11
相关论文
共 40 条
  • [1] Effect of synthesis parameters on catalytic properties of CuO-CeO2
    Avgouropoulos, George
    Ioannides, Theophilos
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 2006, 67 (1-2) : 1 - 11
  • [2] Critical review on the current scenario and significance of crude glycerol resulting from biodiesel industry towards more sustainable renewable energy industry
    Ayoub, Muhammad
    Abdullah, Ahmad Zuhairi
    [J]. RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2012, 16 (05) : 2671 - 2686
  • [3] Production of renewable hydrogen through aqueous-phase reforming of glycerol over Ni/Al2O3-MgO nano-catalyst
    Bastan, Farzad
    Kazemeini, Mohammad
    Larimi, Afsanehsadat
    Maleki, Hesam
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2018, 43 (02) : 614 - 621
  • [4] Aqueous-phase reforming of crude glycerol: effect of impurities on hydrogen production
    Boga, Dilek A.
    Liu, Fang
    Bruijnincx, Pieter C. A.
    Weckhuysen, Bert M.
    [J]. CATALYSIS SCIENCE & TECHNOLOGY, 2016, 6 (01) : 134 - 143
  • [5] Generalised mathematical model to estimate Zn, Pb, Cd, Ni, Cu, Cr and As release from contaminated estuarine sediment using pH-static leaching tests
    Camino Martin-Torre, M.
    Ruiz, Gema
    Galan, Berta
    Viguri, Javier R.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2015, 138 : 780 - 790
  • [6] A laboratory study of producing docosahexaenoic acid from biodiesel-waste glycerol by microalgal fermentation
    Chi, Zhanyou
    Pyle, Denver
    Wen, Zhiyou
    Frear, Craig
    Chen, Shulin
    [J]. PROCESS BIOCHEMISTRY, 2007, 42 (11) : 1537 - 1545
  • [7] Support effects in the aqueous phase reforming of glycerol over supported platinum catalysts
    Ciftci, Aysegul
    Peng, Baoxiang
    Jentys, Andreas
    Lercher, Johannes A.
    Hensen, Emiel J. M.
    [J]. APPLIED CATALYSIS A-GENERAL, 2012, 431 : 113 - 119
  • [8] A review of catalytic aqueous-phase reforming of oxygenated hydrocarbons derived from biorefinery water fractions
    Coronado, I.
    Stekrova, M.
    Reinikainen, M.
    Simell, P.
    Lefferts, L.
    Lehtonen, J.
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (26) : 11003 - 11032
  • [9] A review of catalytic issues and process conditions for renewable hydrogen and alkanes by aqueous-phase reforming of oxygenated hydrocarbons over supported metal catalysts
    Davda, RR
    Shabaker, JW
    Huber, GW
    Cortright, RD
    Dumesic, JA
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 2005, 56 (1-2) : 171 - 186
  • [10] Influence of the nature of the support on the catalytic properties of Pt-based catalysts for hydrogenolysis of glycerol
    Delgado, Severine Noe
    Yap, David
    Vivier, Laurence
    Especel, Catherine
    [J]. JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2013, 367 : 89 - 98