Hydroisomerization of sustainable feedstock in biomass-to-fuel conversion: a critical review

被引:30
作者
Galadima, Ahmad [1 ]
Muraza, Oki [1 ,2 ]
机构
[1] King Fahd Univ Petr & Minerals, Ctr Res Excellence Nanotechnol, Dhahran 30261, Saudi Arabia
[2] King Fahd Univ Petr & Minerals, Dept Chem Engn, Dhahran 30261, Saudi Arabia
关键词
biomass; sustainable feedstock; hydroisomerization; catalysts; LONG N-ALKANES; SUPPORTED MOLYBDENUM CARBIDE; TRANSITION-METAL CARBIDES; HETEROPOLY ACIDS; STEAM GASIFICATION; GAS-PRODUCTION; CATALYTIC CONVERSION; HYDROGEN-PRODUCTION; DEALUMINATED USY; VEGETABLE-OILS;
D O I
10.1002/er.3257
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The production of diesel and gasoline range paraffins from both solid and liquid biomass is one of the promising alternatives being considered for ensuring sustainable fuel supply. Solid biomass gasification produces synthetic gas, which via subsequent Fischer-Tropsch reaction is converted into useful liquid hydrocarbon fuels. Similarly, pyrolysis generates oxygenated and bio-oil products with comparable fuel potentials. The liquid biomass such as vegetable oils, on the other hand can be upgraded by serial hydrogenation, cracking, deoxygenation, and decarboxylation. We have critically reviewed substantial literature on the various conversion processes and the hydroisomerization of the linear bioparaffins into isomerized products with enhanced fuel properties. Emphasis was given to the heterogeneous catalyst systems, operational parameters, reaction mechanisms, and identified challenges. The scope was extended to cover different porous catalysts with prospects in biomass-to-fuel conversion. Copyright (c) 2014 John Wiley & Sons, Ltd.
引用
收藏
页码:741 / 759
页数:19
相关论文
共 195 条
[1]   Thiophene hydrodesulfurization over alumina-supported molybdenum carbide and nitride catalysts: Adsorption sites, catalytic activities, and nature of the active surface [J].
Aegerter, PA ;
Quigley, WWC ;
Simpson, GJ ;
Ziegler, DD ;
Logan, JW ;
McCrea, KR ;
Glazier, S ;
Bussell, ME .
JOURNAL OF CATALYSIS, 1996, 164 (01) :109-121
[2]   Hydroisomerization and hydrocracking of alkanes - Influence of the balance between acid and hydrogenating functions on the transformation of n-decane on PtHY catalysts [J].
Alvarez, F ;
Ribeiro, FR ;
Perot, G ;
Thomazeau, C ;
Guisnet, M .
JOURNAL OF CATALYSIS, 1996, 162 (02) :179-189
[3]   Adaptive neuro-fuzzy inference system and artificial neural network modeling of proton exchange membrane fuel cells based on nanocomposite and recast Nafion membranes [J].
Amirinejad, Mehdi ;
Tavajohi-Hasankiadeh, Naser ;
Madaeni, Sayed Siavash ;
Navarra, Maria Assunta ;
Rafiee, Ezzat ;
Scrosati, Bruno .
INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2013, 37 (04) :347-357
[4]  
[Anonymous], 2009, PNNL18284
[5]  
Antal M.J., 1985, Advances in Solar Energy, P61, DOI DOI 10.1007/978-1-4684-8992-7_3
[6]   Biomass gasification to hydrogen and syngas at low temperature: Novel catalytic system using fluidized-bed reactor [J].
Asadullah, M ;
Ito, S ;
Kunimori, K ;
Yamada, M ;
Tomishige, K .
JOURNAL OF CATALYSIS, 2002, 208 (02) :255-259
[7]   STEAM GASIFICATION OF BIOMASS WITH NICKEL SECONDARY CATALYSTS [J].
BAKER, EG ;
MUDGE, LK ;
BROWN, MD .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1987, 26 (07) :1335-1339
[8]   MECHANISMS OF CATALYTIC BIOMASS GASIFICATION [J].
BAKER, EG ;
MUDGE, LK .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 1984, 6 (03) :285-297
[9]   Thermochemical Routes for Biomass-based Hydrogen Production [J].
Balat, M. .
ENERGY SOURCES PART A-RECOVERY UTILIZATION AND ENVIRONMENTAL EFFECTS, 2010, 32 (15) :1388-1398
[10]   FUNDAMENTAL KINETIC MODELING OF HYDROISOMERIZATION AND HYDROCRACKING ON NOBLE-METAL-LOADED FAUJASITES .1. RATE PARAMETERS FOR HYDROISOMERIZATION [J].
BALTANAS, MA ;
VANRAEMDONCK, KK ;
FROMENT, GF ;
MOHEDAS, SR .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1989, 28 (07) :899-910