Synthesis of Aromatic-Rich Gasoline-Range Hydrocarbons from Biomass-Derived Syngas over a Pd-Promoted Fe/HZSM-5 Catalyst

被引:51
作者
Yan, Qiangu [1 ]
Lu, Yongwu [1 ]
Wan, Caixia [3 ]
Han, Jun [4 ]
Rodriguez, Jose [2 ]
Yin, Jing-Jing [2 ]
Yu, Fei [1 ]
机构
[1] Mississippi State Univ, Dept Agr & Biol Engn, Mississippi State, MS 39762 USA
[2] Mississippi State Univ, Petr Prod Lab, Mississippi State, MS 39762 USA
[3] Univ Missouri, Dept Bioengn, Columbia, MO 65211 USA
[4] Wuhan Univ Sci & Technol, Hubei Key Lab Coal Convers & New Mat, Wuhan 430081, Peoples R China
基金
美国国家科学基金会;
关键词
FISCHER-TROPSCH SYNTHESIS; SUPPORTED RUTHENIUM NANOPARTICLES; ZEOLITE CAPSULE CATALYST; REACTION PERFORMANCE; MIDDLE ISOPARAFFINS; SELECTIVE SYNTHESIS; DEACTIVATION; CONVERSION; HYDRODECHLORINATION; ADSORPTION;
D O I
10.1021/ef402507u
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 aromatic-rich gasoline-range hydrocarbons from wood biomass-derived syngas (biosyngas) was studied by the Fischer-Tropsch synthesis (FTS) over a Pd-promoted Fe/HZSM-5 catalyst. The Pd promoter enhances the catalytic performance of the Fe/HZSM-5 catalyst and promotes the formation of aromatic hydrocarbons. The reaction conditions, i.e., temperature, pressure, and gas hourly space velocity (GHSV), significantly affected the aromatic hydrocarbon selectivity. The higher reaction temperature leads to the higher selectivity toward aromatics in liquid hydrocarbon products. An increase in the reaction pressure also favors the formation of aromatics, but its effect is not as significant as that of the reaction temperature. GHSV has a negative effect on the formation of aromatics because of the short-time contact of the reactant gas with the catalyst. The aromatic hydrocarbon selectivity ranges from 29 to 45%, which is dependent upon the reaction conditions. Aromatic hydrocarbons are mainly composed of xylenes and trimethyl, tetramethyl, and 1,2-dimethyl-3-ethyl benzenes. This study indicates that the Pd-promoted Fe/HZSM-5 catalyst can efficiently convert the biosyngas to aromatic-rich gasoline-range hydrocarbons.
引用
收藏
页码:2027 / 2034
页数:8
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[1]   Catalytic hydrodechlorination of chloroaromatic gas streams promoted by Pd and Ni: The role of hydrogen spillover [J].
Amorim, Claudia ;
Keane, Mark A. .
JOURNAL OF HAZARDOUS MATERIALS, 2012, 211 :208-217
[2]   Hardwood Biomass to Gasoline, Diesel, and Jet Fuel: 1. Process Synthesis and Global Optimization of a Thermochemical Refinery [J].
Baliban, Richard C. ;
Elia, Josephine A. ;
Floudas, Christodoulos A. ;
Gurau, Barri ;
Weingarten, Michael B. ;
Klotz, Stephen D. .
ENERGY & FUELS, 2013, 27 (08) :4302-4324
[3]  
Bao J., 2001, APPL CATAL A-GEN, V394, P195
[4]   A core/shell catalyst produces a spatially confined effect and shape selectivity in a consecutive reaction [J].
Bao, Jun ;
He, Jingjiang ;
Zhang, Yi ;
Yoneyama, Yoshiharu ;
Tsubaki, Noritatsu .
ANGEWANDTE CHEMIE-INTERNATIONAL EDITION, 2008, 47 (02) :353-356
[5]   H-type zeolite coated iron-based multiple-functional catalyst for direct synthesis of middle isoparaffins from syngas [J].
Bao, Jun ;
Yang, Guohui ;
Okada, Chie ;
Yoneyama, Yoshiharu ;
Tsubaki, Noritatsu .
APPLIED CATALYSIS A-GENERAL, 2011, 394 (1-2) :195-200
[6]   LOW-TEMPERATURE HYDROGEN REDUCTION OF PURE CO3O4 AND DOPED WITH PALLADIUM [J].
BELOUSOV, VM ;
STOCH, J ;
BATCHERIKOVA, IV ;
ROZHKOVA, EV ;
LYASHENKO, LV .
APPLIED SURFACE SCIENCE, 1989, 35 (04) :481-494
[7]   Microwave heating during catalyst preparation: influence on the hydrodechlorination activity of alumina-supported palladium-iron bimetallic catalysts [J].
Berry, FJ ;
Smart, LE ;
Prasad, PSS ;
Lingaiah, N ;
Rao, PK .
APPLIED CATALYSIS A-GENERAL, 2000, 204 (02) :191-201
[8]   Syngas adsorption on precipitated iron catalysts reduced by H2, syngas or CO and on those used for high-pressure FT synthesis by in situ diffuse reflectance FTIR spectroscopy [J].
Bian, G ;
Oonuki, A ;
Kobayashi, Y ;
Koizumi, N ;
Yamada, M .
APPLIED CATALYSIS A-GENERAL, 2001, 219 (1-2) :13-24
[9]   Cracking of pentenes to C2-C4 light olefins over zeolites and zeotypes -: Role of topology and acid site strength and concentration [J].
Bortnovsky, O ;
Sazama, P ;
Wichterlova, B .
APPLIED CATALYSIS A-GENERAL, 2005, 287 (02) :203-213
[10]   The addition of HZSM-5 to the Fischer-Tropsch process for improved gasoline production [J].
Botes, FG ;
Böhringer, W .
APPLIED CATALYSIS A-GENERAL, 2004, 267 (1-2) :217-225