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Catalytic process for the transformation of glycerol in inputs for the Petrochemical sector

机译:石油化工行业投入物中甘油转化的催化方法

摘要

This refers to a process of hydrogenation catalytic hydrogenolysis of glycerol / Glycerine or oxygenates and hydrocarbons containing from 1 to 3 carbon ATOMS, using metal catalysts supported on Base Metals of Group VIII of the Periodic Table of B S ElementsWhich were supported by conventional techniques on High specific area Materials, such as Activated Carbon Powder, alumino silicates, aluminates, Clays, zeolites and molecular sieves.Claim 1: process of hydrogenation hydrogenolysis / a load of GLYCERIN or glycerol in which the Reaction occurs in the presence of metal catalysts supported, through the addition of GLYCERIN or glycerol in a hydrogen gas Stream and Cat on the bed Alu00edtico through an Injection pump,Characterized in that it comprises the following steps: a) pretreatment of The Catalyst for Activating the Strip temperature between 150 and 700sc; (b) monitoring of temperature in a reaction Medium between 150 and 550sc; (c) use of pressure in the range between E 0 and 200 kgf / cm2; (d) the addition of GLYCERIN through a jet pump with a molar ratio gliCERINA / H2 between 1: 1000; and (e) the use of a Space Velocity between 0.01 and 100 H - 1, with the aim of achieving the conversion of glycerin.
机译:这是指使用负载在BS元素周期表VIII族贱金属上的金属催化剂对甘油/甘油或含1至3个碳原子的ATOMS的氧化物和含烃的烃进行加氢催化氢解的方法,该方法通过常规技术在高特定区域的材料,例如活性炭粉,铝硅酸盐,铝酸盐,粘土,沸石和分子筛。要求1:氢化氢解过程/负载甘油甘油或甘油的反应在负载的金属催化剂存在下发生,通过在氢气流中添加甘油甘油或甘油,并通过注射泵将催化剂添加到床上的铝上,其特征在于它包括以下步骤:a)预处理催化剂以在150-700sc之间激活带材温度; (b)监测反应介质中温度在150至550sc之间; (c)使用E 0至200 kgf / cm2之间的压力; (d)通过喷射泵以摩尔比gliCERINA / H 2在1:1000之间添加甘油甘油; (e)使用0.01至100H-1的空速,以实现甘油的转化。

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