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CATALYST FOR PROCESS OF METHYLBUTENES DEHYDROGENATION TO ISOPRENE AND METHOD OF ITS LOADING TO REACTOR

机译:甲基丁烯脱氢制异戊​​二烯的催化剂及其负载反应器的方法

摘要

FIELD: chemistry.;SUBSTANCE: catalyst for methylbutenes dehydrogenation to isoprene containing potassium oxide, magnesium oxide, cerium oxide, calcium oxide, molybdenum oxide, silicon dioxide, aluminium oxide and iron oxide is prepared by special high-temperature treatment at 650-1000°C at following components content, wt %: potassium oxide 12.0-19.0; magnesium oxide 1.0-7.0; cerium oxide 2.5-7.0; calcium oxide 2.0-8.0; molybdenum oxide 1.0-3.0; silicon dioxide1.0-2.5; aluminium oxide 0.5-2.0; iron oxide - the rest. The method of the said catalyst loading to the reactor consists in layered charge whereat the upper layer is the said catalyst and lower layer is industrial catalyst of the trade mark K-24I having the following composition, wt %: potassium oxide 10.0-20.0; rubidium or cesium oxide 0.1-5.0; silicon dioxide 10.5-1.2; chromium oxide 2.0-5.0; zirconium dioxide 1.0-3.0; aluminium oxide 0.1-5.0; iron oxide - the rest; the catalyst ratio is in the range from 1:3 to 3:1 respectively.;EFFECT: elaboration of the catalyst for real condition of industrial operation with stable selectivity in the process of methylbutenes dehydrogenation; development of its application method providing maximal yield of the isoprene together with high process selectivity.;2 cl, 10 ex, 2 tbl
机译:领域:化学;物质:通过在650-1000°C下进行特殊的高温处理,制备含有氧化钾,氧化镁,氧化铈,氧化钙,氧化钼,二氧化硅,氧化铝和氧化铁的甲基丁烯脱氢成异戊二烯的催化剂C在以下组分含量下,wt%:氧化钾12.0-19.0;氧化镁1.0-7.0;氧化铈2.5-7.0;氧化钙2.0-8.0;氧化钼1.0-3.0;二氧化硅1.0-2.5;氧化铝0.5-2.0;氧化铁-其余。所述催化剂装入反应器的方法为分层装料,其中上层为所述催化剂,下层为商标K-24I的工业催化剂,其组成如下,重量%:氧化钾10.0-20.0; 0.1或氧化铯0.1-5.0;二氧化硅10.5-1.2;氧化铬2.0-5.0;二氧化锆1.0-3.0;氧化铝0.1-5.0;氧化铁-其余;效果:在甲基丁烯脱氢过程中,以稳定的选择性为工业操作的实际条件精制催化剂;应用方法的开发,可提供最高产量的异戊二烯以及高工艺选择性。; 2 cl,10 ex,2 tbl

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