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METHOD FOR HYDROGENIZING ACETONE IN ISOPROPYL ALCOHOL

机译:异丙醇中丙酮的加氢方法

摘要

FIELD: technological processes.;SUBSTANCE: present invention relates to a method for the hydrogenation of acetone to isopropyl alcohol, which is widely used as an octane additive to gasolines, anti-icing fluid, solvent in the production of surfactants, plasticizers, additives to oils, medicines. Hydrogenation is carried out with a hydrogenating gas, in which hydrogen-containing exhaust gas is used after pyrolysis of a hydrocarbon feedstock and separation of propylene and ethylene, characterized by the following composition and concentration limits of the components, %: hydrogen – 40–90, nitrogen – 7.7–23.5, methane – 27–45, carbon dioxide – up to 1, carbon monoxide – up to 1.5, admixture of olefins – up to 3, diene hydrocarbons – up to 2.5, oxygen – up to 0.5, in the presence of a hydrogenation catalyst on a neutral carrier, the use of copper in the amount of 10–30 wt.%, deposited on a carrier in the form of silica gel granules with a grain size of 2.8–7.0 mm, specific surface area of 290–330 m2/g – the rest, which is activated at a temperature of 150–180 °C, in a current of a mixture of hydrogen:nitrogen=1:1 by volume for 2–3 hours, then in a stream of hydrogen for 0.5 hours. Hydrogenation of acetone is carried out at a temperature of 100–195 °C, pressure 20–30 atm, molar ratio hydrogen:acetone=(2–5):1, and hydrogenating gas before mixing with acetone is subjected to precontact preparation at a temperature of 150–250 °C and a pressure of 20–30 atm in the zone of the reactor of precontact preparation filled with the same catalyst.;EFFECT: proposed method allows to obtain the target product with a high yield using hydrogen-containing gas with oxygen, olefinic and diene hydrocarbon impurities.;1 cl, 3 tbl, 27 ex
机译:丙酮加氢制异丙醇的方法技术领域本发明涉及一种丙酮加氢制异丙醇的方法,该方法被广泛用作汽油,防冰液,溶剂的辛烷值添加剂,用于生产表面活性剂,增塑剂,添加剂。油,药品。用氢化气体进行氢化,其中在烃原料热解并分离丙烯和乙烯后,使用含氢废气,其特征在于以下组分的组成和浓度极限,%:氢– 40–90 ,氮气中7.7 – 23.5,甲烷– 27–45,二氧化碳–最多1,一氧化碳–最多1.5,烯烃的混合物–最多3,二烯烃–最多2.5,氧气–最多0.5。在中性载体上存在氢化催化剂时,使用10–30 wt。%的铜,以2.8–7.0 mm粒径的硅胶颗粒形式沉积在载体上,比表面积为290–330 m 2 / g –其余部分在150:180°C的温度下在氢气:氮气= 1:1体积比为2的混合气体中被激活3小时,然后在氢气流中0.5小时。丙酮的氢化反应是在100–195°C的温度,20–30 atm的压力,氢气与丙酮的摩尔比=(2–5):1进行的,在与丙酮混合之前,对氢化气体进行预接触制备。填充相同催化剂的预接触制备反应器区域的温度为150–250°C,压力为20–30 atm 。;效果:建议的方法允许使用含氢气体以高收率获得目标产物含氧,烯烃和二烯烃杂质。; 1 cl,3 tbl,27 ex

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