Structured ZSM-5/SiC foam catalysts for bio-oils upgrading

被引:26
作者
Ou, Xiaoxia [1 ]
Wu, Chunfei [2 ]
Shi, Kaiqi [3 ]
Hardacre, Christopher [1 ]
Zhang, Jinsong [4 ]
Jiao, Yilai [4 ]
Fan, Xiaolei [1 ]
机构
[1] Univ Manchester, Sch Engn, Dept Chem Engn & Analyt Sci, Oxford Rd, Manchester M13 9PL, Lancs, England
[2] Queens Univ Belfast, Sch Chem & Chem Engn, Belfast BT7 1NN, Antrim, North Ireland
[3] Univ Nottingham Ningbo China, New Mat Inst, Ningbo 315100, Peoples R China
[4] Chinese Acad Sci, Inst Met Res, Shenyang Natl Lab Mat Sci, 72 Wenhua Rd, Shenyang 110016, Peoples R China
基金
欧盟地平线“2020”; 英国工程与自然科学研究理事会; 中国国家自然科学基金;
关键词
ZSM-5; SiC foam; Bio-oils upgrading; Coke formation; Deactivation mechanism; Process intensification; BIOMASS FAST PYROLYSIS; MODEL COMPOUNDS; ZEOLITE H-ZSM-5; HZSM-5; ZEOLITE; COKE FORMATION; LIGHT OLEFINS; METHANOL; COATINGS; CRACKING; CONVERSION;
D O I
10.1016/j.apcata.2020.117626
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
ZSM-5 zeolite coating supported on SiC foams was prepared by a precursor dispersion-secondary growth method and the resulting structured ZSM-5/SiC foam catalyst was used for the proof-of-concept study of catalytic bio-oils upgrading (Le. deoxygenation of the model compounds of methanol and anisole) in reference to ZSM-5 catalyst pellets. A layer of ZSM-5 coating with inter-crystal porosity on SiC foams was produced by curing the zeolite precursor thermally at 80 degrees C. The use of SiC foam as the zeolite support significantly improved transport phenomena compared to the packed-bed using ZSM-5 pellets, explaining the comparatively good catalytic performance achieved by the structured ZSM-5/SiC foam catalyst. In comparison with the ZSM-5 pellets, the ZSM-5/SiC foam catalyst showed 100.0% methanol conversion (at the weight hourly space velocity, WHSV, of 8 h(-1)) and 100.0% anisole conversion (at WHSV =5 h(-1)) at the initial stage of the processes, while only about 3% were obtained for the ZSM-5 pellets, under the same conditions. Based on the comparative analysis of the characterisation data on the fresh and spent catalysts, the deactivation mechanisms of the ZSM-5/SiC and the ZSM-5 pellet catalysts were explained. The process intensification using SiC foam to support ZSM-5 improved the global gas-to-solid mass transfer notably, and hence mitigating the pore blocking due to the carbon deposition on the external surface of supported ZSM-5.
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页数:9
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