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Effect of process variables on product yield distribution in thermal catalytic cracking of naphtha to light olefins over Fe/HZSM-5

机译:Fe / HZSM-5上石脑油热催化裂解制烯烃过程中工艺变量对产物收率分布的影响

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摘要

The effect of temperature, WHSV and Fe loading over HZSM-5 catalyst in thermal-catalytic cracking (TCC) of naphtha for the production of light olefins has been studied. The response surface defined by three most significant parameters is obtained from Box-Behnken design method and the optimal parameter set is found. The results show that ethylene increases with temperature, while propylene shows an optimum at 650 °C. Moderate WHSV is favorable for maximum production of light olefins. Addition of Fe to HZSM-5 has a favorable effect on the production of light olefins up to 6% of loading. Excess amount of loading decreases the conversion of naphtha, which leads to a drop in light olefin yields. The yield of light olefins (ethylene and propylene) at 670 ℃, 44 hr~(-1) and 6 wt% Fe has been increased to 5.43 wt% compared to the unmodified HZSM-5 and reaches to 42.47 wt%.
机译:研究了HZSM-5催化剂上温度,WHSV和Fe负载量对石脑油热催化裂化生产轻质烯烃的HZSM-5催化剂的影响。通过Box-Behnken设计方法获得了由三个最重要参数定义的响应面,并找到了最佳参数集。结果表明,乙烯随温度增加,而丙烯在650°C时表现最佳。适中的WHSV有利于最大程度地生产轻质烯烃。将铁添加到HZSM-5中对高达6%负载的轻质烯烃的生产具有有利的影响。过量的负载降低了石脑油的转化率,这导致轻质烯烃产率的下降。与未改性的HZSM-5相比,在670℃,44 hr〜(-1)和6 wt%的Fe下,轻烯烃(乙烯和丙烯)的收率提高到5.43 wt%,达到42.47 wt%。

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