Cracking of a rapeseed vegetable oil under realistic FCC conditions

被引:172
作者
Dupain, Xander
Costa, Daniel J.
Schaverien, Colin J.
Makkee, Michiel
Moulijn, Jacob A.
机构
[1] Delft Univ Technol, Sect Reactor & Catalysis Engn, Fac Sci Appl, NL-2628 BL Delft, Netherlands
[2] Shell Global Solut Int BV, NL-1031 CM Amsterdam, Netherlands
关键词
fluid catalytic cracking (FCC); vegetable oil; rapeseed oil; oleic acid; stearic acid;
D O I
10.1016/j.apcatb.2006.10.005
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
A rapeseed vegetable oil, pure and blended with conventional FCC feedstock, has been catalytically cracked with a commercial equilibrium catalyst under realistic FCC conditions. The rapeseed oil can be converted into gasoline- and diesel-range hydrocarbons that are low in sulfur and nitrogen. The triglycerides are predominately converted within 50 ms at 485-585 degrees C into fatty acids through radical cracking reactions. Relatively high amounts of coke are formed. The high aromatisation rate of the fatty acids causes the formation of large amounts of aromatics of up to 30-40 wt.% in the gasoline fraction. Due to the high aromaticity the product is hardly subject to serial cracking reactions and the lower olefins yield (C-3(=) and C-4(=)) remains low. The rate of aromatisation is highly dependent on the olefinicity of the fatty acid and the reaction temperature. The catalytic conversion of the carbon-carbon bond saturated stearic acid results in a higher gasoline yield (57 wt.% versus 34 wt.% for the rapeseed oil) with a much lower aromaticity (13 wt.% in gasoline versus 32 wt.% in gasoline for the rapeseed oil). Due to the lower aromaticity the serial cracking reactions to the lower olefins are much better (7 wt.% C-3(=) and 7 wt.% C-4(=)). In all cases, the oxygen from the fatty acids is evolved predominantly as water. Other oxygenates have not been observed in significant quantities. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:44 / 61
页数:18
相关论文
共 41 条
[1]   Adsorption and catalytic reaction in FCC catalysts using a novel fluidized CREC riser simulator [J].
Atias, JA ;
de Lasa, H .
CHEMICAL ENGINEERING SCIENCE, 2004, 59 (22-23) :5663-5669
[2]   Renewable fuels and chemicals by thermal processing of biomass [J].
Bridgwater, AV .
CHEMICAL ENGINEERING JOURNAL, 2003, 91 (2-3) :87-102
[3]  
Colthup N. B., 1990, INTRO INFRARED RAMAN
[4]   THE CHEMISTRY OF CATALYTIC CRACKING [J].
CORMA, A ;
WOJCIECHOWSKI, BW .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1985, 27 (01) :29-150
[5]   A new continuous laboratory reactor for the study of catalytic cracking [J].
Corma, A ;
Martínez, C ;
Melo, FV ;
Sauvanaud, L ;
Carriat, JY .
APPLIED CATALYSIS A-GENERAL, 2002, 232 (1-2) :247-263
[6]   Overview of applications of biomass fast pyrolysis oil [J].
Czernik, S ;
Bridgwater, AV .
ENERGY & FUELS, 2004, 18 (02) :590-598
[7]   Potential applications of renewable energy sources, biomass combustion problems in boiler power systems and combustion related environmental issues[ [J].
Demirbas, A .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2005, 31 (02) :171-192
[8]   Biomass and wastes: Upgrading alternative fuels [J].
Demirbas, A ;
Demirbas, MF .
ENERGY SOURCES, 2003, 25 (04) :317-329
[9]   Production of clean transportation fuels and lower olefins from Fischer-Tropsch Synthesis waxes under fluid catalytic cracking conditions - The potential of highly paraffinic feedstocks for FCC [J].
Dupain, X ;
Krul, RA ;
Schaverien, CJ ;
Makkee, M ;
Moulijn, JA .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2006, 63 (3-4) :277-295
[10]   Optimal conditions in fluid catalytic cracking: A mechanistic approach [J].
Dupain, X ;
Makkee, M ;
Moulijn, JA .
APPLIED CATALYSIS A-GENERAL, 2006, 297 (02) :198-219