Steam reforming of model bio-oil compounds 2-butanone, 1-methoxy-2-propanol, ethyl acetate and butyraldehyde over Ni/Al2O3

被引:12
作者
Baviskar, Chetana V. [1 ]
Vaidya, Prakash D. [1 ]
机构
[1] Inst Chem Technol, Dept Chem Engn, Nathalal Parekh Rd, Bombay 400019, Maharashtra, India
关键词
Hydrogen; Reforming; Nickel; 2-Butanone; 1-Methoxy-2-propanol; Ethyl acetate; Butyraldehyde; HYDROGEN-PRODUCTION; PRODUCE HYDROGEN; ACETIC-ACID; BIOMASS; CATALYST; KINETICS; GASIFICATION; ETHANOL; BUTANOL; WASTE;
D O I
10.1016/j.ijhydene.2017.07.063
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
Oil derived from fast pyrolysis of biomass (or bio-oil) is a candidate renewable feedstock for producing hydrogen (H-2). In this work, the steam reforming of model oxygenates present in the bio-oil aqueous fraction was studied in a fixed-bed reactor. Using Ni/Al2O3 catalyst, the reactions with 2-butanone, 1-methoxy-2-propanol, ethyl acetate and butyraldehyde were studied. To study the efficacy of the chosen catalyst for H-2 production, experiments were performed in the 623-773 K range using varying steam/carbon ratios in feed (15-25 mol/mol). The conversion of the various feeds was of the order: butyraldehyde > ethyl acetate > 1-methoxy-2-propanol > 2-butanone. The catalyst was characterized using SEM, XRD, TPR/TPD and TGA methods. It showed high stability for 7 h of time-on-stream. (C) 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:21667 / 21676
页数:10
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