Isopropanol decomposition on carbon based acid and basic catalysts

被引:60
作者
Bedia, J. [1 ]
Rosas, J. M. [1 ]
Vera, D. [1 ]
Rodriguez-Mirasol, J. [1 ]
Cordero, T. [1 ]
机构
[1] Univ Malaga, Dept Chem Engn, Sch Ind Engn, E-29071 Malaga, Spain
关键词
Isopropanol; Dehydration; Dehydrogenation; Carbon catalyst; BIOMASS PYROLYSIS OIL; ACTIVATED CARBONS; OXYGENATE COMPONENTS; ALPO4; CATALYSTS; HZSM-5; ZEOLITE; DEHYDRATION; ADSORPTION; 2-PROPANOL; CONVERSION; DEHYDROGENATION;
D O I
10.1016/j.cattod.2010.04.043
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Chemical activation of biomass waste with different activating agents allows the preparation of activated carbons with a relatively highly porous development and different surface chemistry properties. Acidic and basic carbon based catalysts have been prepared by chemical activation of olive stone waste with H3PO4 and H2SO4 of acid character and Ca(OH)(2) and Ba(OH)(2) of basic character. The carbons have been tested as catalysts for the isopropanol decomposition reaction. The acidic carbons show higher steady state conversions than those corresponding to the basic carbons. The highest conversions were obtained using the carbon activated with phosphoric acid as catalyst. In the absence of oxygen acidic carbon based catalysts dehydrate isopropanol to propylene. In the case of the basic carbon catalysts, the carbon activated with Ba(OH)(2) mainly dehydrogenates isopropanol to acetone, with low production of propylene. The carbon activated with Ca(OH)(2) presents acid and basic surface sites and propylene and acetone are obtained on this catalyst. In the presence of oxygen, the acidic carbons show higher conversion values and part of the isopropanol suffers oxidative dehydrogenation yielding acetone as well as propylene, although at high isopropanol steady state conversion values only propylene is obtained. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:89 / 96
页数:8
相关论文
共 44 条
[1]   Catalytic conversion of a biofuel to hydrocarbons: Effect of mixtures of HZSM-5 and silica-alumina catalysts on product distribution [J].
Adjaye, JD ;
Katikaneni, SPR ;
Bakhshi, NN .
FUEL PROCESSING TECHNOLOGY, 1996, 48 (02) :115-143
[2]  
BANSAL RC, 1988, ACTIVE CARBON, pCH2
[3]   N-alkylation of aniline with methanol over CrPO4 and CrPO4-AlPO4 (5-50 wt% AlPO4) catalysts [J].
Bautista, FM ;
Campelo, JM ;
Garcia, A ;
Luna, D ;
Marinas, JM ;
Romero, AA ;
Urbano, MR .
JOURNAL OF CATALYSIS, 1997, 172 (01) :103-109
[4]   A kinetic study of 2-propanol dehydration on carbon acid catalysts [J].
Bedia, J. ;
Ruiz-Rosas, R. ;
Rodriguez-Mirasol, J. ;
Cordero, T. .
JOURNAL OF CATALYSIS, 2010, 271 (01) :33-42
[5]  
BEDIA J, 2010, AICHE J, V271, P33
[6]   Preparation and characterization of carbon based acid catalysts for the dehydration of 2-propanol [J].
Bedia, Jorge ;
Maria Rosas, Juana ;
Marquez, Josefa ;
Rodriguez-Mirasol, Jose ;
Cordero, Tomas .
CARBON, 2009, 47 (01) :286-294
[7]  
Bellamy L.J., 1980, The Infrared Spectra of Complex MoleculesAdvances in Infrared Group Frequencies, VVolume 2
[8]   DETERMINATION OF PROTON ACIDITY OF SOLID CATALYSTS BY CHROMATOGRAPHIC ADSORPTION OF STERICALLY HINDERED AMINES [J].
BENESI, HA .
JOURNAL OF CATALYSIS, 1973, 28 (01) :176-178
[9]   GC/MS characterization of liquids generated from low-temperature pyrolysis of wood [J].
Branca, C ;
Giudicianni, P ;
Di Blasi, C .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (14) :3190-3202
[10]   Adsorption of gases in multimolecular layers [J].
Brunauer, S ;
Emmett, PH ;
Teller, E .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1938, 60 :309-319