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In-situ production of valuable aromatics via pyrolysis of waste polypropylene using commercial catalyst ZSM-5

机译:利用商业催化剂ZSM-5通过热解溶解废聚丙烯的有价值芳烃的原位生产

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摘要

Waste polypropylene has been subjected to pyrolysis followed by in-situ aromatization in a specially designed semi batch reactor at the temperature ranging from 500 - 800°C. The molecules of interest are valuable aromatics benzene, toluene, ethyl benzene and xylene (BTEX) which appeared highest amount in the liquid mixture. The catalyst used is commercial ZSM-5 (30:1). The catalytic pyrolysis of PP is studied in a semi batch reactor in two different phases, keeping the catalyst in the liquid phase (L-type) and liquid and vapor phase/multiphase (M-type), respectively. The BTEX yield is enhanced significantly using multiphase catalytic pyrolysis of polypropylene. The catalytic performance of ZSM-5 catalyst for PP pyrolysis is evaluated with respect to target aromatics BTEX. The thermal pyrolysis of PP produced maximum liquid yield of 80.56 wt. % at a temperature of 700°C. The commercial catalysts ZSM-5 produced highest liquid yield of 86.3 wt. % for liquid phase (L-type) pyrolysis. The BTEX yield is significantly increased from 30.9 wt.% for thermal pyrolysis to 53.09 wt. % for catalytic multiphase/M-type pyrolysis. Almost 72 % increase in BTEX yield is recorded for catalytic multiphase/M-type pyrolysis in comparison to thermal process. The pyrolysis oil is analyzed using GC-FID, carbon residue test and other fuel testing methods to examine the suitability of its end use and aromatic content.
机译:废物聚丙烯已经进行了热解,然后在特殊设计的半批量反应器中在500-800℃的温度下原位芳族化。感兴趣的分子是有价值的芳烃苯,甲苯,乙苯和二甲苯(BTEX),其在液体混合物中出现了最高量。使用的催化剂是商业ZSM-5(30:1)。在两个不同相的半批量反应器中研究了PP的催化热解,分别将催化剂保持在液相(L型)和液相和气相/多相(M型)中。使用聚丙烯的多相催化热解显着提高了BTEX产率。关于靶芳烃BTEX评价PP热解的ZSM-5催化剂的催化性能。 PP的热热解产生最大液体产率80.56重量%。 %在700°C的温度下。商业催化剂ZSM-5产生的最高液体产率为86.3重量%。液相(L型)热解的%。 BTEX产量从30.9重量%增加。%热解水量至53.09重量%。催化多相/ m型热解的%。与热过程相比,对催化多相/ M型热解记录了BTEX产量的近72%。通过GC-FID,碳残留试验和其他燃料试验方法分析热解油,以检查其最终使用和芳族含量的适用性。

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