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LOW PRESSURE HYDROGENATION OF HEAVY OIL RESIDUES

机译:重油残渣的低压加氢

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Processing of heavy oil residues with high content of sulphur and heavy metals is of great importance and practical interest. Process of the liquid phase hydrogenolysis of residues obtained from atmospheric or vacuum oil processing using a catalytic additive of the soluble metal (VI-VIII group) salts solution dispersed into the raw material was developed in Russia.The catalytic system is formed in a reaction zone at the contact of the additive with hot hydrogen. The sizes of both catalytical particles and raw materials are approximately equal. This fact provides reliable contacts of the phases and allow to decrease working pressure.The optimal parameters of the process were determined on a pilot plant with output 1 ton/h, duration test was 10-30 days. Different raw materials were used.Hydrogenolysis of tar was realised at 430-450 °C under low pressure <7 MPa at a mass rate of 1-3 h~(-1), and recycling of the process residues 30-50% with use of activating additives. Coke production in the system was not observed.A project of industrial plant with power 0.5-1 mln ton a year including devices for catalytic additive preparation, hydrogenolysis of raw material, demetallation and utilization of the process residues, has been worked out.
机译:具有高硫和重金属含量的重油渣油的加工具有重要意义和实际意义。俄罗斯开发了利用常压或真空油加工工艺处理的残留物的液相氢解工艺,该工艺使用分散在原材料中的可溶性金属(VI-VIII基)盐溶液的催化添加剂进行。 在添加剂与热氢接触的反应区中形成催化体系。催化颗粒和原料的尺寸大致相等。这一事实提供了各相的可靠接触,并允许降低工作压力。 该工艺的最佳参数是在产量为1吨/小时的中试工厂上确定的,持续时间为10-30天。使用了不同的原料。 焦油的氢化反应是在430-450°C的低压下<7 MPa以1-3 h〜(-1)的质量比进行的,并使用活化添加剂将工艺残渣循环使用30-50%。没有观察到系统中的焦炭产生。 已设计出一个年产0.5-1万吨的工业装置项目,其中包括催化添加剂的制备,原料的氢解,脱金属和工艺残渣的利用。

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