Chemistry of Furan Conversion into Aromatics and Olefins over HZSM-5: A Model Biomass Conversion Reaction

被引:289
作者
Cheng, Yu-Ting [1 ]
Huber, George W. [1 ]
机构
[1] Univ Massachusetts, Dept Chem Engn, Goessmann Lab 159, Amherst, MA 01003 USA
来源
ACS CATALYSIS | 2011年 / 1卷 / 06期
关键词
furan; catalytic fast pyrolysis; biomass; aromatics; olefins; zeolites; HZSM-5; hydrocarbon pool; TEMPERATURE-PROGRAMMED DESORPTION; CATALYTIC FAST PYROLYSIS; FIXED-BED REACTOR; LIQUID FUEL; BIO-OIL; PRODUCT DISTRIBUTION; DESIGN PARAMETERS; ZEOLITE; HYDROCARBONS; ADSORPTION;
D O I
10.1021/cs200103j
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
The conversion of furan (a model of cellulosic biomass) over HZSM-5 was investigated in a thermogravimetric analysis-mass spectrometry system, in situ Fourier transform infrared analysis, and in a continuous-flow fixed-bed reactor. Furan adsorbed as oligomers at room temperature with a 1.73 of adsorbed furan/A1 ratio. These oligomers were polycyclic aromatic compounds that were converted to CO, CO2, aromatics, and olefins at temperatures from 400 to 600 degrees C. Aromatics (e:g:, benzene, toluene, and naphthalene), oligomer isomers (e.g., benzofuran, 2,2-methylenebisfuran, and benzodioxane), and heavy oxygenates (C12+ oligomers) were identified as intermediates formed inside HZSM-5 at different reaction temperatures. During furan conversion, graphite-type coke formed on the catalyst surface, which caused the aromatics and olefins formation to deactivate within the first 30 mm of time on stream We have measured the effects of space velocity and temperature for furan conversion to help us understand the chemistry of biomass conversion inside zeolite catalysts. The major products for furan conversion included CO, CO2, allene, C-2-C-6 olefins, benzene, toluene, styrene, benzofuran, indene, and naphthalene. The aromatics (benzene and toluene) and olefins (ethylene and propylene) selectivity decreased with increasing space velocity. Unsaturated hydrocarbons such as allene, cyclopentadiene, and aromatics selectivity increased with increasing space velocity. The product distribution was selective to olefins and CO at high temperatures (650 degrees C) but was selective to aromatics (benzene and toluene) at intermediate temperatures (450-600 degrees C). At low temperatures (450 degrees C), benzofuran and coke contributed 60% of the carbon selectivity. Several different reactions were occurring for furan conversion over zeolites. Some important reactions that we have identified in this study include Diels-Alder condensation (e.g., two furans form benzofuran and water), decarbonylation (e.g., furan forms CO and allene), oligomerization (allene forms olefins and aromatics plus hydrogen), and alkylation (e.g., furan plus olefins). The product distribution was far from thermodynamic equilibrium.
引用
收藏
页码:611 / 628
页数:18
相关论文
共 50 条
  • [41] Effects of HZSM-5 crystallite size on stability and alkyl-aromatics product distribution from conversion of propanal
    Hoang, Trung Q.
    Zhu, Xinli
    Lobban, Lance L.
    Resasco, Daniel E.
    Mallinson, Richard G.
    CATALYSIS COMMUNICATIONS, 2010, 11 (11) : 977 - 981
  • [42] Enhanced aromatics selectivity and stability in a coaromatization reaction over P/[ZnCr]/HZSM-5
    Lv, Junmin
    Wang, Dan
    Zhu, Bing
    Li, Haibo
    Fan, Subing
    Zhao, Tian-sheng
    REACTION CHEMISTRY & ENGINEERING, 2023, 8 (05) : 1015 - 1022
  • [43] Catalytic Conversion of Furan to Hydrocarbons using HZSM-5: Coking Behavior and Kinetic Modeling including Coke Deposition
    Shao, Shanshan
    Zhang, Huiyan
    Xiao, Rui
    Shen, Dekui
    ENERGY TECHNOLOGY, 2017, 5 (01) : 111 - 118
  • [44] Enhanced Performance of Methyl Ester to Renewable Aromatics via Thermocatalytic Conversion over Metal-Modified HZSM-5 Zeolites: An Experimental Study
    Bayat, Ahmad
    CHEMISTRYSELECT, 2018, 3 (47): : 13338 - 13344
  • [45] In situ catalytic conversion of biomass fast pyrolysis vapors on HZSM-5
    Zhang, Yindi
    Chen, Ping
    Lou, Hui
    JOURNAL OF ENERGY CHEMISTRY, 2016, 25 (03) : 427 - 433
  • [46] Catalytic conversion of acetol over HZSM-5 catalysts-influence of Si/Al ratio and introduction of mesoporosity
    Eschenbacher, Andreas
    Andersen, Jakob Afzali
    Jensen, Anker Degn
    CATALYSIS TODAY, 2021, 365 : 301 - 309
  • [47] Conversion of canola oil and canola oil methyl ester (CME) to green aromatics over a HZSM-5 catalyst: a comparative study
    Bayat, A.
    Sadrameli, S. M.
    RSC ADVANCES, 2015, 5 (36) : 28360 - 28368
  • [48] Pulsed streamer discharge plasma over Ni/HZSM-5 catalysts for methane conversion to aromatics at atmospheric pressure
    Li, Xiao-Song
    Shi, Chuan
    Xu, Yong
    Zhang, Xiu-Ling
    Wang, Kang-Jun
    Zhu, Ai-Min
    PLASMA PROCESSES AND POLYMERS, 2007, 4 (01) : 15 - 18
  • [49] Catalytic conversion of anisole over HY and HZSM-5 zeolites in the presence of different hydrocarbon mixtures
    Prasomsri, Teerawit
    To, Anh T.
    Crossley, Steven
    Alvarez, Walter E.
    Resasco, Daniel E.
    APPLIED CATALYSIS B-ENVIRONMENTAL, 2011, 106 (1-2) : 204 - 211
  • [50] Conversion of Industrial Feedstock mainly with Butanes and Butenes over HZSM-5 and Zn/HZSM-5 (nitrate) Catalysts
    Maftei, Dan
    Asaftei, Iuliean Vasile
    Sandu, Ion
    Manea, Liliana Rozemarie
    Birsa, Lucian Mihail
    Earar, Kamel
    REVISTA DE CHIMIE, 2015, 66 (05): : 673 - 680