Pyrolysis of plastic waste and scrap tyres in a fluid bed reactor

Walter Kaminsky
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引用次数: 39

Abstract

An outline of laboratory-scale investigations of pyrolysis is followed by a description of pilot-scale experiments designed to exploit the raw material content of polymeric substances rather than their heating value merely as fuels. Dependent on the feed material, gaseous products (40–60 wt.%, e.g. hydrogen, methane, ethylene, ethane) as well as liquid products (40–60 wt.%, mainly simple aromatics) are obtained. The gas is sufficient to heat the process.

Fluid sand beds are surprisingly insensitive to the unit size of the feed material, so that scrap tyres can be pyrolyzed as a whole to avoid the cost of size reduction. Carbon soot and fillers are separated in a cyclone and metal pieces can be removed from the inclined bottom of the reactor. Results for a 2 Mg/day pilot plant are presented and a preview of a 4000 Mg/year plant is given, for which cost—benefit calculations are compared with those of some other scrap tyre pyrolysis processes.

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在流化床反应器中热解废塑料和废轮胎
实验室规模的热解研究的大纲,随后描述了中试规模的实验,旨在利用聚合物物质的原料含量,而不是仅仅作为燃料的热值。根据原料的不同,可以得到气态产物(40-60 wt.%,如氢、甲烷、乙烯、乙烷)和液态产物(40-60 wt.%,主要是简单芳烃)。气体足以加热这一过程。令人惊讶的是,流体砂床对进料的单位尺寸不敏感,因此废轮胎可以作为一个整体进行热解,以避免尺寸减小的成本。碳烟和填料在旋风中分离,金属碎片可以从反应器的倾斜底部去除。介绍了一个2 Mg/天的中试工厂的结果,并对一个4000 Mg/年的工厂进行了预览,并与其他一些废轮胎热解工艺的成本效益计算进行了比较。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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Editorial Contents The role of pyrolysis in the disposal of waste tyres Energy and materials requirements of primary aluminium production in the U.K. A methane production feasibility model for central anaerobic digesters
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