温度对HDPE在Ni/Ce/Al2O3上催化热解的影响

V. Balasundram, N. Ibrahim, R. Isha
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摘要

本文主要研究了反应温度对高密度聚氨酯(HDPE)在Ni/Ce/Al2O3上催化热解生成裂解油气富集烃的影响。实验采用原位固定床反应器,在500、600、700和800℃4种不同的热解反应温度下进行。以Al2O3 (75% wt.%)为载体,镍(20% wt.%)和铈(5% wt.%)为促进剂,采用初湿浸渍法。在所研究的所有样品中,催化剂与塑料的质量比保持恒定在1:1。结果表明,Ni/Ce/Al2O3催化剂对HDPE的催化热解具有协同作用,热解油中烃类化合物(C5 ~ C20)收率高,热解气中氢气组分高。热解油在700℃时收率最高(53.23%),热解气在800℃时收率最高(67.85%)。在500 ~ 800℃范围内,热解油中的小分子烃(C5 ~ C9)随温度升高而减少。氢气产率最高可达77.59%。在700℃下得到。因此,本研究从塑料废物流中生产有价值的替代能源具有经济可行性。
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The Effect of Temperature on Catalytic Pyrolysis of HDPE Over Ni/Ce/Al2O3
The main objective of the current work is to investigate the influence of reaction temperature on catalytic pyrolysis of High-Density Polyurethane (HDPE) over Ni/Ce/Al2O3 into enriched hydrocarbons of pyrolytic oil and gas The experiments were performed at four different pyrolysis reaction temperatures (500, 600, 700, and 800 °C) via in-situ fixed bed reactor. The Al2O3 (75 wt.%) was used as a support, while nickel (20 wt.%) and cerium (5 wt.%) were impregnated as promoters via incipient wetness impregnation method. The catalyst to plastic mass ratio was kept constant at 1:1 for all investigated samples. The results revealed that the Ni/Ce/Al2O3 catalyst has synergistic effects on the catalytic pyrolysis of HDPE into a high yield of hydrocarbon compounds (C5 – C20) in pyrolytic oil and hydrogen gas composition in pyrolytic gas. The highest yield of pyrolytic oil was achieved at 700 °C (53.23 %), while the highest yield of pyrolytic gas was achieved at 800 °C (67.85 %). The small molecular hydrocarbons in pyrolytic oil (C5 - C9) decreases with increasing temperature from 500 to 800 °C. The highest hydrogen gas yield of 77.59 %. was achieved at 700 °C. Thus, this research has economic feasibility in producing alternative valuable energy from the plastic waste stream.
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