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首页> 外文期刊>Catalysis science & technology >Theta-1 zeolite catalyst for increasing the yield of propene when cracking olefins and its potential integration with an olefin metathesis unit
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Theta-1 zeolite catalyst for increasing the yield of propene when cracking olefins and its potential integration with an olefin metathesis unit

机译:θ1沸石催化剂增加产量丙烯的裂解烯烃及其可能与烯烃复分解的集成单位

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摘要

There is a need for on-purpose propene production technologies beyond energy-intensive steam cracking. Hexene is a compound with limited value that can be found in several streams in the refinery and can readily crack on zeolites at lower temperatures and shorter contact times than those used for cracking alkanes. Cracking over ZSM-5 zeolite yields high selectivity to light olefins. These results are improved by Theta-1 zeolite, which can yield a remarkable propene molar selectivity of 180% (90 wt%) at 90% conversion, close to the maximum thermodynamic yield. Moreover, crystal engineering allowed its TOF to increase by more than 50%. Based on these results we also identified some prospective applications of Theta-1 zeolite as a catalyst for an integrated process directed to maximize propene.
机译:需要刻意的丙烯生产技术在能源密集型的蒸汽破解。可以发现在几个流炼油厂和沸石在容易裂缝较低的温度和较短的接触时间那些用于烷烃。ZSM-5沸石收益率高选择性烯烃。沸石,可以产生显著的丙烯摩尔的选择性180% (90 wt %)为90%转换,接近最大热力学产量。TOF增加50%以上。我们还发现了一些潜在的结果θ1沸石作为催化剂的应用一个集成的过程直接最大化丙烯。

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