以SiO2为催化剂热催化裂解废管橡胶的非常规燃料

Riaz Muhammad , Felizitas Schlederer , Ali Riaz
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引用次数: 0

摘要

每年都有大量的废旧橡胶材料被丢弃,其中大部分来自汽车废旧轮胎和内胎橡胶,造成了令人极为关切的环境问题,对世界各地的废物管理机构构成了严峻的挑战。已经提出了各种方法来纠正这些问题,并不时加以应用。热解提供了一个很有前途的解决方案,将废轮胎转化为潜在的燃料和化学品。热催化热解是一种成熟的工艺,旨在回收材料,能源或化学产品。对生产有用产品的废管和橡胶等材料的需求和需要是这类废物的一个有价值的考虑因素,这反过来又可以最大限度地减少对自然资源的依赖。内胎橡胶主要由异丁烯-异戊二烯制成,对环境有危害。然而,也有机会将这种废物转化为有价值的能源。本文报道了以二氧化硅(SiO2)为催化剂,对异丁烯-异戊二烯橡胶催化热解成液体燃料的温度、时间、催化剂重量等参数的优化。在温度为350℃,催化剂(SiO2)用量为1.5 g,加热时间为1小时的优化条件下,橡胶的最大转化率为油。得到的热解产物进行了多次物理和化学测试。报告的结果证实存在30%的脂肪烃,25%的极性烃和40%的芳香烃。蒸馏数据表明,得到的油与柴油一样是芳烃和烯烃的混合物,可以用作替代燃料。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Non-Conventional fuels from thermocatalytic pyrolysis of waste tube rubber using SiO2 as catalyst

Non-Conventional fuels from thermocatalytic pyrolysis of waste tube rubber using SiO2 as catalyst
Large quantities of used rubber material, mostly from vehicle scrap tires and tube rubbers, are discarded every year, causing environmental problems of great concern and representing a tough challenge for waste management bodies around the world. Various ways to remediate the issues have been proposed and applied from time to time. Pyrolysis offers a promising solution to convert waste tires into potential fuels and chemicals. Thermo-catalytic pyrolysis is a well-established process that aims for material, energy or chemical product recovery. The demand and need for the use of materials like scrap tubes and rubbers for producing useful products is a valuable consideration for this kind of waste that in turn may minimize the dependency on natural resources. Inner tube rubber, which is mainly made of isobutylene-isoprene, poses a hazard to the environment. However, there is also an opportunity to turn this waste product into a valuable energy source. In the current study optimization of parameters such as temperature, time and catalyst weight for catalytic pyrolysis of isobutylene-isoprene rubber into liquid fuel in the presence of Silicon Dioxide (SiO2) as catalyst is reported. A maximum rubber conversion into oils was obtained at optimized conditions of 350 °C temperature, 1.5 g of catalyst (SiO2) for an hour heating time. The obtained pyrolyzed products were subjected to several physical and chemical tests. Reported results confirm the presence of 30 % of aliphatic hydrocarbons, 25 % polar hydrocarbons and 40 % aromatic hydrocarbons. The distillation data indicates that oil obtained is a mixture of aromatic and olefinic hydrocarbons as that of diesel and may be used as an alternative fuel.
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