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THREE STAGE CATALYTIC TREATMENT, UNDER HYDROGEN PRESSURE OF HIGHLY UNSATURATED HEAVY CUTS

机译:在高度不饱和重切氢的氢气压力下进行三阶段催化处理

摘要

specific disclosure.the invention relates to a hydrogenation processoutbreak of a hydrocarbon fraction from a fluid.operation of heating, hot, for the most part, beyondc and containing more than 80% by weight of oil aromati -products and more than 0.01% by weight of sulphur. in this process, wefirst of all, to move the unstable fraction oilwith hydrogen in contact with a catalyst containing athe metal of the group viii, at a temperature of 50 to 300 c. we treatthe product obtained with hydrogen in contact with acatalyst containing at least one metal of each of the groups.via and viii at a temperature of 250 to 400 c are discussed finally.the product obtained with 200 new ii by hydrogencontact with a catalyst containing 0.1 to 2% by weight of at least onenoble metal of group viii, 0.5 to 15% by weight of chlorine orfluoride and alumina. we collect a fractionhydrogenated oil and stabilized. the process ofthe invention enables to significantly increasethe yield of ethylene in a steam cracking.
机译:具体的披露。本发明涉及一种氢化方法从流体中爆发出碳氢化合物馏分。加热操作,绝大部分c并含有超过80%(重量)的芳香油-产品和超过0.01%(重量)的硫。在这个过程中,我们首先,移动不稳定馏分油与氢气接触的催化剂中含有在50至300℃的温度下,第vi族金属。我们对待与氢接触得到的产物催化剂,其每组包含至少一种金属。最后讨论了温度在250至400摄氏度之间的过孔和过孔。氢用200 new ii获得的产物与含有0.1至2%重量的至少一种的催化剂接触vi族贵金属,氯含量为0.5至15%(重量)或氟化物和氧化铝。我们收集一小部分氢化油并稳定。的过程本发明能够显着增加蒸汽裂解中乙烯的收率。

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