Ethanol CO2 reforming on La2O3 and CeO2-promoted Cu/Al2O3 catalysts for enhanced hydrogen production

被引:31
|
作者
Shafiqah, Mohd-Nasir Nor [1 ]
Hai Nguyen Tran [2 ]
Trinh Duy Nguyen [3 ]
Phuong, Pham T. T. [4 ]
Abdullah, Bawadi [5 ]
Lam, Su Shiung [6 ]
Phuong Nguyen-Tri [7 ]
Kumar, Ravinder [8 ]
Nanda, Sonil [9 ]
Vo, Dai-Viet N. [3 ]
机构
[1] Univ Malaysia Pahang, Fac Chem & Nat Resources Engn, Kuantan 26300, Pahang, Malaysia
[2] Duy Tan Univ, Inst Fundamental & Appl Sci, Ho Chi Minh City 700000, Vietnam
[3] Nguyen Tat Thanh Univ, Ctr Excellence Green Energy & Environm Nanomat CE, 300A Nguyen Tat Thanh,Dist 4, Ho Chi Minh City 755414, Vietnam
[4] Vietnam Acad Sci & Technol, Inst Chem Technol, 1 Mac Dinh Chi Str,Dist 1, Ho Chi Minh City, Vietnam
[5] Univ Teknol Petronas, Ctr Biofuel & Biochem Res, Chem Engn Dept, Biomass Proc Lab, Bandar Seri Iskandar 32610, Perak, Malaysia
[6] Univ Malaysia Terengganu, Sch Ocean Engn, Eastern Corridor Renewable Energy Grp, Pyrolysis Technol Res Grp, Terengganu 21030, Malaysia
[7] Univ Montreal, Dept Chem, Montreal, PQ, Canada
[8] Macquarie Univ, Dept Environm Sci, Sydney, NSW 2109, Australia
[9] Univ Western Ontario, Dept Chem & Biochem Engn, London, ON, Canada
关键词
Ethanol CO2 reforming; CeO2; La2O3; Cu-based catalysts; Syngas; Hydrogen; SYNGAS PRODUCTION; PARTIAL OXIDATION; NI/SBA-15; CATALYSTS; NI CATALYSTS; STEAM; METHANE; CARBON; PERFORMANCE; CEO2; TEMPERATURE;
D O I
10.1016/j.ijhydene.2019.10.024
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
3%Ce- and 3%La-promoted 10%Cu/Al2O3 catalysts were synthesized via a sequential incipient wetness impregnation approach and implemented for ethanol CO2 reforming (ECR) at 948-1023 K and stoichiometric feed ratio. CeO2 and La2O3 promoters reduced CuO crystallite size from 32.4 to 27.4 nm due to diluting impact and enhanced the degree of reduction of CuO -> Cu-0. Irrespective of reaction temperature, 3%La-10%CuAl2O3 exhibited the highest reactant conversions, H-2 and CO yields followed by 3%Ce-10% Cu/Al2O3 and 10%Cu/Al2O3. The greatest C2H5 OH and CO2 conversions of 87.6% and 55.1%, respectively were observed on 3%La-10%Cu/Al2O3 at 1023 K whereas for all catalysts, H-2/CO ratios varying from 1.46 to 1.91 were preferred as feedstocks for Fischer-Tropsch synthesis. Activation energy for C2H5OH consumption was also reduced with promoter addition from 53.29 to 47.05 kJ mol(-1). The thorough CuO -> Cu-0 reduction by H-2 activation was evident and the Cu-0 active phase was resistant to re-oxidation during ECR for all samples. Promoters addition reduced considerably the total carbon deposition from 40.04% to 27.55% and greatly suppressed non-active graphite formation from 26.94% to 4.20% because of their basic character and cycling redox enhancement. (C) 2019 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:18398 / 18410
页数:13
相关论文
共 50 条
  • [41] Hydrogen production by steam reforming of ethanol over Ni/Al2O3-La2O3 xerogel catalysts
    Song, Ji Hwan
    Yoo, Sangbeom
    Yoo, Jaekyeong
    Park, Seungwon
    Gim, Min Yeong
    Kim, Tae Hyeop
    Song, In Kyu
    MOLECULAR CATALYSIS, 2017, 434 : 123 - 133
  • [42] Role of La2O3 as Promoter and Support in Ni/γ-Al2O3 Catalysts for Dry Reforming of Methane
    Al-Fatesh, Ahmed S.
    Naeem, Muhammad A.
    Fakeeha, Anis H.
    Abasaeed, Ahmed E.
    CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2014, 22 (01) : 28 - 37
  • [43] Syngas production by CO2 reforming of ethanol over Ni/Al2O3 catalyst
    Hu, Xun
    Lu, Gongxuan
    CATALYSIS COMMUNICATIONS, 2009, 10 (13) : 1633 - 1637
  • [44] Production of Syngas from Ethanol CO2 Reforming on La-doped Cu/Al2O3: Impact of Promoter Loading
    Shafiqah, Mohd-Nasir Nor
    Trinh Duy Nguyen
    Jun, Lau N.
    Bahari, Mahadi B.
    Phuong, Pham T. T.
    Abdullah, Bawadi
    Vo, Dai-Viet N.
    6TH INTERNATIONAL CONFERENCE ON ENVIRONMENT (ICENV 2018): EMPOWERING ENVIRONMENT AND SUSTAINABLE ENGINEERING NEXUS THROUGH GREEN TECHNOLOGY, 2019, 2124
  • [45] K-, CeO2-, and Mn-promoted Ni/Al2O3 catalysts for stable CO2 reforming of methane
    Nandini, A
    Pant, KK
    Dhingra, SC
    APPLIED CATALYSIS A-GENERAL, 2005, 290 (1-2) : 166 - 174
  • [46] Steam Reforming of C2-C4 Alkanes Over Ni–(CeO2, La2O3)–Al2O3/Cordierite Catalysts
    Ie. V. Gubareni
    Ya. P. Kurilets
    S. O. Soloviev
    Theoretical and Experimental Chemistry, 2016, 52 : 323 - 330
  • [47] Autothermal reforming of propane for hydrogen production over Pd/CeO2/Al2O3 catalysts
    Faria, Wagner L. S.
    Dieguez, Lidia C.
    Schmal, Martin
    APPLIED CATALYSIS B-ENVIRONMENTAL, 2008, 85 (1-2) : 77 - 85
  • [48] Hydrogen production by steam reforming of ethanol over Co3O4/La2O3/CeO2 catalysts synthesized by one-step polymerization method
    Carvalho, Flavio L. S.
    Asencios, Yvan J. O.
    Rego, Ana M. B.
    Assaf, Elisabete M.
    APPLIED CATALYSIS A-GENERAL, 2014, 483 : 52 - 62
  • [49] Hydrogen production through CO2 reforming of methane over Ni/CeZrO2/Al2O3 catalysts
    Faria, E. C.
    Neto, R. C. R.
    Colman, R. C.
    Noronha, F. B.
    CATALYSIS TODAY, 2014, 228 : 138 - 144
  • [50] Catalytic activity and characterization of Ni/Al2O3 and NiK/Al2O3 catalysts for CO2 methane reforming
    Juan-Juan, J
    Román-Martínez, MC
    Illán-Gómez, MJ
    APPLIED CATALYSIS A-GENERAL, 2004, 264 (02) : 169 - 174