Hydrogen production from aqueous-phase reforming of glycerol, sorbitol, and glycine over Pt/Al2O3 catalyst in a fixed-bed reactor

被引:0
|
作者
Kalekar, Vinayak N. [1 ]
Vaidya, Prakash D. [1 ]
机构
[1] Inst Chem Technol, Dept Chem Engn, Nathalal Parekh Marg, Mumbai 400019, India
关键词
aqueous-phase reforming; biomass; hydrogen; kinetics; platinum; OXYGENATED HYDROCARBONS; RENEWABLE HYDROGEN; H-2; PRODUCTION; GAMMA-ALUMINA; STEAM; XYLITOL; ALKANES; POLYOLS; PT/C; CEO2;
D O I
10.1002/kin.21752
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
Aqueous-phase reforming (APR) is an interesting technique for generating hydrogen (H-2) from biofeeds. In this work, APR of model compounds of wet biomass for H-2 production was investigated. Glycerol, sorbitol, and glycine were the chosen model compounds. They represent polyols and amino acids in wet biomass such as waste sludge and microalgal biomass. The Pt/Al2O3 catalyst was preferred and it was characterized using nitrogen adsorption-desorption, scanning electron microscopy (SEM), transmission electron microscopy (TEM), x-ray diffraction (XRD), and x-ray photoelectron spectroscopy (XPS) techniques. APR trials were performed in a continuous fixed-bed reactor. The reaction conditions chosen for this work were: temperature (T) 453-498 K, pressure (P) 1.2-2.4 MPa, feed concentration 5-15 wt%, and weight hourly space velocity (WHSV) 0.15-0.6 g reactant/(g catalyst h). The best conditions for H-2 production by the APR process were found to be T = 498 K, P = 2.4 MPa, and feed concentration = 15 wt%. Among the chosen model compounds, glycerol exhibited the highest H-2 selectivity (82.7%) and H-2 yield (21.6%) at 498 K. The analysis of kinetic data suggested first-order reaction kinetics for all the model compounds. The values of activation energy for the reactions with glycerol (55.4 kJ/mol), sorbitol (51.6 kJ/mol), and glycine (45.7 kJ/mol) were determined. Thus, APR is a promising route for effectively producing H-2-bearing gaseous products with high heating value from wet biomass.
引用
收藏
页码:674 / 686
页数:13
相关论文
共 50 条
  • [41] Renewable hydrogen production by aqueous-phase reforming of Glycerol using Ni/Al2O3-MgO nano-catalyst: effect of the Ni loading
    Farzad Bastan
    Mohammad Kazemeini
    Biomass Conversion and Biorefinery, 2023, 13 : 237 - 246
  • [42] Hydrogen Production via Glycerol Dry Reforming over La-Ni/Al2O3 Catalyst
    Siew, Kah Weng
    Lee, Hua Chyn
    Gimbun, Jolius
    Cheng, Chin Kui
    BULLETIN OF CHEMICAL REACTION ENGINEERING AND CATALYSIS, 2013, 8 (02) : 160 - 166
  • [43] Hydrogen production from glycerol dry reforming over Ag-promoted Ni/Al2O3
    Harun, Norazimah
    Abidin, Sumaiya Zainal
    Osazuwa, Osarieme Uyi
    Taufiq-Yap, Yun Hin
    Azizan, Mohammad Tazli
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2019, 44 (01) : 213 - 225
  • [44] Glycerol steam reforming over Ni-Fe-Ce/Al2O3 catalyst for hydrogen production
    Go, Gwang Sub
    Lee, Hong Joo
    Moon, Dong Ju
    Kim, Young Chul
    RESEARCH ON CHEMICAL INTERMEDIATES, 2016, 42 (01) : 289 - 304
  • [45] Lanthanum Effect on Ni/Al2O3 as a Catalyst Applied in Steam Reforming of Glycerol for Hydrogen Production
    Sanchez, Nuria
    Maria Encinar, Jose
    Nogales, Sergio
    Felix Gonzalez, Juan
    PROCESSES, 2019, 7 (07) : 1 - 18
  • [46] Aqueous phase reforming of sorbitol over Ca doped Ni/Al2O3 for value-added chemicals production
    Radzi, Mohamad Razlan Md
    Azizan, Mohammad Tazli
    Daud, Nur Fatin Dariah Mohamad
    Topek, Muhammad Azizi
    Abidin, Sumaiya Zainal
    MATERIALS TODAY-PROCEEDINGS, 2018, 5 (10) : 21728 - 21736
  • [47] Characterization and Catalytic Properties of the Ni/Al2O3 Catalysts for Aqueous-phase Reforming of Glucose
    Wen, Guodong
    Xu, Yunpeng
    Xu, Zhusheng
    Tian, Zhijian
    CATALYSIS LETTERS, 2009, 129 (1-2) : 250 - 257
  • [48] Experimental studies and comprehensive reactor modeling of hydrogen production by the catalytic reforming of crude ethanol in a packed bed tubular reactor over a Ni/Al2O3 catalyst
    Aboudheir, A
    Akande, A
    Idem, R
    Dalai, A
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2006, 31 (06) : 752 - 761
  • [49] Methane Dry Reforming over Ni-Co/Al2O3: Kinetic Modelling in a Catalytic Fixed-bed Reactor
    Benguerba, Yacine
    Virginie, Mirella
    Dumas, Christine
    Ernst, Barbara
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2017, 15 (06)
  • [50] Highly stable Pt/CoAl2O4 catalysts in Aqueous-Phase Reforming of glycerol
    Reynoso, A. J.
    Iriarte-Velasco, U.
    Gutierrez-Ortiz, M. A.
    Ayastuy, J. L.
    CATALYSIS TODAY, 2021, 367 : 278 - 289