Production of coke from scrap tire vacuum pyrolysis oil

被引:50
作者
CHaala, A [1 ]
Roy, C [1 ]
机构
[1] UNIV LAVAL,DEPT GENIE CHIM,QUEBEC CITY,PQ G1K 7P4,CANADA
关键词
vacuum; pyrolysis; tire; oil; coke; electrode;
D O I
10.1016/0378-3820(95)00065-8
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The heavy fraction (b.p. > 350 degrees C) of the oil obtained during vacuum pyrolysis of used tires is mainly composed of aromatic hydrocarbons. The possibility to use this fraction as a raw material in the coke industry was investigated. The coking experiments were carried out in a laboratory scale reactor at a temperature of 480-500 degrees C under the partial pressure formed by the vapors and gas produced. The heating temperature rate was 10 degrees C/min. It was found that one ton of tires can generate 28 kg of coke. The coke obtained is low in sulfur and ash and has a low metal content. The main contaminant of petroleum coke, vanadium, is not present in the pyrolytic coke. These characteristics rank the tire-derived coke obtained among the best needle coke or graphite coke base-materials. A characterization of the gas and liquid by-product fractions as well as the coke obtained was performed. High quality products were obtained.
引用
收藏
页码:227 / 239
页数:13
相关论文
共 31 条
[1]  
AKHMETOV MM, 1986, KHIM TEKH TOPL MACEL, V1, P6
[2]  
BIKTIMIROVA TG, 1990, SB NAUCH T BASHK N I, V29, P91
[3]  
BLACKMAN LCF, 1970, MODERN ASPECTS GRAPH, P320
[4]  
BUZNOWSKA B, 1990, KOKS SMOLA GAZ, V35, P151
[5]  
GUEORGUYEV ZI, CHIM TEKH TOPL MACEL, V7, P22
[6]  
HADARSHAN SV, 1994, FUEL, V73, P962
[7]   UPGRADING OF DELAYED AND FLUID COKES FROM OIL SAND BY DESULFURIZATION [J].
HALL, ES ;
TOLLEFSON, EL ;
GEORGE, ZM ;
SCHNEIDER, L .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1982, 60 (03) :418-424
[8]  
HULISZ S, 1991, NAFTA, V46, P85
[9]   UPGRADING OF OIL SAND COKE RESIDUES [J].
ITYOKUMBUL, MT .
FUEL PROCESSING TECHNOLOGY, 1994, 38 (02) :127-138
[10]  
JACOB RR, 1971, HYDROCARB PROCESS, V50, P132