Kinetics of scrap tyre pyrolysis under fast heating conditions

被引:75
作者
Aguado, R [1 ]
Olazar, M [1 ]
Vélez, D [1 ]
Arabiourrutia, M [1 ]
Bilbao, J [1 ]
机构
[1] Univ Basque Country, Dept Ingn Quim, E-48080 Bilbao, Spain
关键词
pyrolysis kinetics; tyres; recycling; hydrocarbon formation;
D O I
10.1016/j.jaap.2005.02.006
中图分类号
O65 [分析化学];
学科分类号
070302 [分析化学]; 081704 [应用化学];
摘要
The kinetics of scrap tyre pyrolysis has been studied by means of thermogravimetry (runs at constant temperature and following temperature ramps) and using a fast heating microreactor. The advantages of the microreactor for obtaining kinetic data at higher temperatures (in the 773-973 K range) than those corresponding to thermogravimetry and under conditions similar to those of continuous large-scale reactor are clearly shown. The validity of the kinetic parameters determined (E = 98.6 U mol(-1) and k(0) = 7.35 x 10(4) s(-1)) Will only be restricted by unavoidable heat and mass transfer limitations, which have been minimized by using a particle size smaller than 0.2 mm. The kinetic results are evidence, on the one hand, of the limitations of these laboratory techniques for the kinetic study and, on the other, of the inherent heat and mass limitations of this material. Through monitoring by gas chromatography, the kinetics of formation of hydrocarbon products has been determined. These products are interesting as raw materials for petrochemistrical industry (mainly light olefins and aromatics) and for the synthesis of basic materials in tyre manufacturing (isoprene and 1,3-butadiene). (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:290 / 298
页数:9
相关论文
共 56 条
[1]
Kinetic study of polyolefin pyrolysis in a conical spouted bed reactor [J].
Aguado, R ;
Olazar, M ;
Gaisán, B ;
Prieto, R ;
Bilbao, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (18) :4559-4566
[2]
Pyrolysis of sawdust in a conical spouted bed reactor.: Yields and product composition [J].
Aguado, R ;
Olazar, M ;
José, MJS ;
Aguirre, G ;
Bilbao, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (06) :1925-1933
[3]
A model for primary and heterogeneous secondary reactions of wood pyrolysis [J].
Ahuja, P ;
Kumar, S ;
Singh, PC .
CHEMICAL ENGINEERING & TECHNOLOGY, 1996, 19 (03) :272-282
[4]
ALLOTT K, 1991, PROCESS ENG ENV PROT, P45
[5]
KINETICS OF CELLULOSE PYROLYSIS IN NITROGEN AND STEAM [J].
ANTAL, MJ ;
FRIEDMAN, HL ;
ROGERS, FE .
COMBUSTION SCIENCE AND TECHNOLOGY, 1980, 21 (3-4) :141-152
[6]
EFFECTS OF REACTOR SEVERITY ON THE GAS-PHASE PYROLYSIS OF CELULOSE-DERIVED AND KRAFT LIGNIN-DERIVED VOLATILE MATTER [J].
ANTAL, MJ .
INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1983, 22 (02) :366-375
[7]
KINETIC-ANALYSIS OF LIGNIN PYROLYSIS USING NON-ISOTHERMAL TGA DATA [J].
AVNI, E ;
COUGHLIN, RW .
THERMOCHIMICA ACTA, 1985, 90 (AUG) :157-167
[8]
CHARACTERIZATION OF PYROLYTIC LIGHT NAPHTHA FROM VACUUM PYROLYSIS OF USED TIRES - COMPARISON WITH PETROLEUM NAPHTHA [J].
BENALLAL, B ;
ROY, C ;
PAKDEL, H ;
CHABOT, S ;
POIRIER, MA .
FUEL, 1995, 74 (11) :1589-1594
[9]
THE DEGRADATION OF GUAYULE RUBBER AND THE EFFECT OF RESIN COMPONENTS ON DEGRADATION AT HIGH-TEMPERATURE [J].
BHOWMICK, AK ;
RAMPALLI, S ;
GALLAGHER, K ;
SEEGER, R ;
MCINTYRE, D .
JOURNAL OF APPLIED POLYMER SCIENCE, 1987, 33 (04) :1125-1139
[10]
KINETICS OF THERMAL-DECOMPOSITION OF CELLULOSE .1. INFLUENCE OF EXPERIMENTAL CONDITIONS [J].
BILBAO, R ;
ARAUZO, J ;
MILLERA, A .
THERMOCHIMICA ACTA, 1987, 120 :121-131