Biomass to olefins: Cracking of renewable naphtha

被引:85
作者
Pyl, Steven P. [1 ]
Schietekat, Carl M. [1 ]
Reyniers, Marie-Francoise [1 ]
Abhari, Ramin [2 ]
Marin, Guy B. [1 ]
Van Geem, Kevin M. [1 ]
机构
[1] Ghent Univ LCT, Chem Technol Lab, B-9052 Ghent, Belgium
[2] Syntroleum Corp, Tulsa, OK USA
关键词
Biomass conversion; Olefin production; Steam cracking; Comprehensive 2D GC; 2-DIMENSIONAL GAS-CHROMATOGRAPHY; STEAM CRACKING; COKE FORMATION; DIMETHYL DISULFIDE; THERMAL-CRACKING; RELATIVE RATES; HYDROCARBONS; PYROLYSIS; MECHANISM; SEVERITY;
D O I
10.1016/j.cej.2011.04.062
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
An alternative route for the production of light olefins is proposed starting from low value and waste fats, greases and other renewable fractions. The first step catalytically converts triglycerides and/or fatty acids from bio oils to a high quality paraffinic diesel or jet fuel and renewable naphtha. GC x GC-TOF-MS and GC x GC-FID characterization of the renewable naphtha showed that it mainly consists of n-paraffins (32.6 wt%) and iso-paraffins (60 wt%), with only small amounts of aromatics (0.8 wt%), naphthenics (6.3 wt%) and olefinics (0.3 wt%). No remaining oxygenates are measured, making it a potentially attractive feed for the production of ethylene. Steam cracking of this renewable naphtha in a pilot plant revealed that high light olefin yields can be obtained (ethylene yield of 31 wt% and a propylene yield of 17.5 wt%), while the amount of pyrolysis gasoline (15 wt%) and pyrolysis fuel oil (<1 wt%) produced remains small. An experimental coking study further confirmed the attractive character of this feed. Run length simulations show that higher run lengths can be expected in comparison with the typically used naphtha fractions from fossil resources. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:178 / 187
页数:10
相关论文
共 51 条
[1]  
Abhari R, 2009, BIORENEWABLE NAPHTHA
[2]  
Abhari R, 2009, HYDRODEOXYGENATION P
[3]  
Abhari R, 2008, PROCESS COPRODUCING
[4]  
Adahchour M., 2008, J CHROMATOGRAPHY A, P1186
[5]  
Bechtel, 2003, GASIFICATION PLANT C
[6]  
Beens J, 1998, HRC-J HIGH RES CHROM, V21, P47
[7]   Fouling phenomena in pyrolysis and combustion processes [J].
Bozzano, G ;
Dente, M ;
Faravelli, T ;
Ranzi, E .
APPLIED THERMAL ENGINEERING, 2002, 22 (08) :919-927
[8]   Recent advancements in ethylene and propylene production using the UOP/Hydro MTO process [J].
Chen, JQ ;
Bozzano, A ;
Glover, B ;
Fuglerud, T ;
Kvisle, S .
CATALYSIS TODAY, 2005, 106 (1-4) :103-107
[9]   Oxidative pyrolysis of ethane [J].
Chen, Q ;
Schweitzer, EJA ;
VandenOosterkamp, PF ;
Berger, RJ ;
DeSmet, CRH ;
Marin, GB .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (08) :3248-3251
[10]  
Consultants T., 2005, GRIDL ETH DEM PROJ U