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Increasing the selectivity of the hydrocarbon feedstock pyrolysis

机译:增加烃类原料热解的选择性

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The process of hydrocarbon feedstock pyrolysis is the principal method used to produce ethylene which is a primary product utilized in the fabrication of plastic materials, synthetic resins, fibers and other similar products. The current level of process capacity and the necessity to steadily increase the petrochemical industry's potential make the problem of improving the efficiency of the process an urgent one. The aim of the present work in terms of the pyrolysis mechanism analysis is to develop a method of increasing the pyrolysis selectivity for ethylene with minimal hydrogen consumption. It was shown on the base of established relative reactivity of different type C-H bonds in the reactions of interaction with H atoms and CH3 radicals, that the selectivity of the hydrogen atoms and methyl radicals in the substitution reactions at high temperatures are notably different. This makes possible a new method of controlling the selectivity of ethylene formation based solely on the influence of the concentration ratio of the chain carrier radicals [H]:[CH3] in the reaction mixture on the reaction output irrespective of changes in temperature, pressure and contact time. The minimum amount of hydrogen required to produce the desired effect was estimated.
机译:碳氢化合物原料热解过程是生产乙烯的主要方法,乙烯是制造塑料,合成树脂,纤维和其他类似产品时使用的主要产品。当前的工艺能力水平和稳定增加石化工业潜力的必要性使得提高工艺效率的问题成为迫在眉睫的问题。就热解机理分析而言,本工作的目的是开发一种以最小的氢消耗来提高对乙烯的热解选择性的方法。基于在与H原子和CH 3自由基相互作用的反应中建立的不同类型的C-H键的相对反应性,表明在高温下的取代反应中氢原子和甲基自由基的选择性显着不同。这使得一种仅基于反应混合物中链载体自由基[H]:[CH3]的浓度比对反应产量的影响而控制乙烯形成选择性的新方法成为可能,而与温度,压力和压力的变化无关。联系时间。估计产生所需效果所需的最小氢量。

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