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首页> 外文期刊>Applied Catalysis, A. General: An International Journal Devoted to Catalytic Science and Its Applications >Dilution effect of the feed on yield of olefins during catalytic cracking of vacuum gas oil
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Dilution effect of the feed on yield of olefins during catalytic cracking of vacuum gas oil

机译:减压瓦斯油催化裂化过程中进料对烯烃收率的稀释作用

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A vacuum gas oil has been co-fed with nitrogen at different partial pressures in a microacitivity (MAT) unit. The cracking rate versus hydrocarbon partial pressure can be fitted to a first-order kinetic rate equation. On the other hand, hydrogen transfer reactions, which follow second-order kinetics, are more affected than conversion by the decrease in hydrocarbon partial pressure, resulting in an increase in the yield of propylene and in general of LPG olefins. The decrease in conversion, due to the lowering of hydrocarbon partial pressure, could be compensated by a mechanical mixing effect introduced by the dilution gas that improves feed vaporization and mixing. It will be shown that a MAT unit can be used to show both effects separately, i.e. feed dilution and feed dispersion. (C) 2002 Elsevier Science B.V. All rights reserved. [References: 8]
机译:真空瓦斯油已在微分活性(MAT)单元中以不同的分压与氮气共同进料。裂化速率与烃分压的关系可以拟合为一阶动力学速率方程。另一方面,遵循二级动力学的氢转移反应比转化率受烃分压降低的影响更大,从而导致丙烯(通常是LPG烯烃)的收率增加。由于烃分压的降低,转化率的降低可以通过稀释气体引入的机械混合作用来补偿,该混合作用改善了进料的汽化和混合。将显示MAT单元可用于分别显示两种作用,即饲料稀释和饲料分散。 (C)2002 Elsevier Science B.V.保留所有权利。 [参考:8]

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