Catalytic conversion of commingled polymer waste into chemicals and fuels over spent FCC commercial catalyst in a fluidised-bed reactor

被引:57
作者
Lin, Y. -H. [1 ]
Yang, M. -H.
机构
[1] Kao Yuan Univ, Dept Biochem Engn, Kaohsiung 821, Taiwan
[2] Kao Yuan Univ, Grad Inst Environm Polymer Mat, Kaohsiung 821, Taiwan
关键词
polymer waste; fluidised-bed reactor; catalyst; pyrolysis; selectivity; HIGH-DENSITY POLYETHYLENE; CRACKING CATALYSTS; SILICA-ALUMINA; HEAVY OIL; DEGRADATION; PYROLYSIS; POLYPROPYLENE; PLASTICS; HZSM-5; POLYOLEFINS;
D O I
10.1016/j.apcatb.2006.07.005
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 commingled post-consumer polymer (CPW#1) was pyrolysed overspent fluid catalytic cracking (FCC) commercial catalyst (ECat-1) using a laboratory fluidised-bed reactor operating isothermally at ambient pressure. The influence of reaction conditions including catalyst, temperature, ratios of commingled polymer to catalyst feed and flow rates of fluidising gas was examined. The conversion for spent FCC commercial catalyst (82.7 wt%) gave much higher yield than silicate (only 14.2 wt%) and the highest yield (nearly 87 wt%) was obtained for ZSM-5. Greater product selectivity was observed with ECat-1 as a recycled catalyst with about 56 wt% olefins products in the C-3-C-7 range. The selectivity could be further influenced by changes in reaction conditions. Valuable hydrocarbons of olefins and iso-olefins were produced by low temperatures and short contact times used in this study. It is also demonstrated that the use of spent FCC commercial catalyst and under appropriate reaction conditions can have the ability to control both the product yield and product distribution from polymer degradation, potentially leading to a cheaper process with more valuable products. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:145 / 153
页数:9
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