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Frontiers in Energy

ISSN 2095-1701

ISSN 2095-1698(Online)

CN 11-6017/TK

Postal Subscription Code 80-972

2018 Impact Factor: 1.701

Front. Energy    2022, Vol. 16 Issue (3) : 492-501    https://doi.org/10.1007/s11708-021-0721-8
RESEARCH ARTICLE
Steam reforming of toluene as a tar model compound with modified nickel-based catalyst
Omeralfaroug KHALIFA1, Mingxin XU1, Rongjun ZHANG2, Tahir IQBAL3, Mingfeng LI2, Qiang LU1()
1. State Key Laboratory of Alternate Electric Power System with Renewable Energy Sources, North China Electric Power University, Beijing 102206, China
2. Research Institute of Petroleum Processing, SINOPEC, Beijing 100083, China
3. Faculty of Agricultural Engineering and Technology, PMAS-Arid Agriculture University, Rawalpindi, Pakistan
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Abstract

Catalytic steam reforming is a promising route for tar conversion to high energy syngas in the process of biomass gasification. However, the catalyst deactivation caused by the deposition of residual carbon is still a major challenge. In this paper, a modified Ni-based Ni-Co/Al2O3-CaO (Ni-Co/AC) catalyst and a conventional Ni/Al2O3 (Ni/A) catalyst were prepared and tested for tar catalytic removal in which toluene was selected as the model component. Experiments were conducted to reveal the influences of the reaction temperature and the ratio between steam to carbon on the toluene conversion and the hydrogen yield. The physicochemical properties of the modified Ni-based catalyst were determined by a series of characterization methods. The results indicated that the Ni-Co alloy was determined over the Ni-Co/AC catalyst. The doping of CaO and the presence of Ni-Co alloy promoted the performance of toluene catalytic dissociation over Ni-Co/AC catalyst compared with that over Ni/A catalyst. After testing in steam for 40 h, the carbon conversion over Ni-Co/AC maintained above 86% and its resistance to carbon deposition was superior to Ni/A catalyst.

Keywords catalytic steam reforming      tar model compound      Ni-based catalyst      carbon resistance     
Corresponding Author(s): Qiang LU   
Online First Date: 05 February 2021    Issue Date: 07 July 2022
 Cite this article:   
Omeralfaroug KHALIFA,Mingxin XU,Rongjun ZHANG, et al. Steam reforming of toluene as a tar model compound with modified nickel-based catalyst[J]. Front. Energy, 2022, 16(3): 492-501.
 URL:  
https://academic.hep.com.cn/fie/EN/10.1007/s11708-021-0721-8
https://academic.hep.com.cn/fie/EN/Y2022/V16/I3/492
Fig.1  Schematic diagram of experimental setup for catalytic steam reforming of toluene.
Fig.2  Effect of temperatures.
Fig.3  Effects of temperatures on gas compositions.
Fig.4  Effect of S/C ratios.
Fig.5  Stability tests of Ni/A and Ni-Co/AC catalysts.
Catalyst Specific surface area/(m2·g1) Pore volume/(cm3·g1) Average pore diameter/nm Particle size Dp*/nm
Ni/A Fresh 196.66 0.60 15.38 25.5
Aged 89.08 0.26 7.90 27.25
Ni-Co/AC Fresh 50.71 0.22 23.65 23.41
Aged 35.61 0.21 20.07 25.24
Tab.1  Structural properties of the fresh and the aged Ni/A and Ni-Co/AC catalysts
Fig.6  XRD patterns of the catalysts. (a) Fresh Ni/A; (b) fresh Ni-Co/AC; (c) aged Ni/A; (d) aged Ni-Co/AC.
Fig.7  H2-TPR profiles.
Fig.8  XPS spectra of Ni 2p over fresh and aged catalysts.
Catalyst Ni0/(Ni0 + Ni2+)/% Decrement/%
Ni/A Fresh 18.00 9.4
Aged 16.30
Ni-Co/AC Fresh 32.64 4.1
Aged 31.14
Tab.2  Percentage concentration of Ni species in Ni/A and Ni-Co/AC catalysts
Catalyst Deposited carbon/(wt.%) Conversion decrement/%
Ni/A 72.63 14.7
Ni-Co/AC 19.16 7.48
Tab.3  Carbon contents and conversion decrement (700°C, S/C= 2.5, and GHSV= 20000 h1)
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