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CATALYST FOR ISOMERIZATION OF C4-C7-ALKANE HYDROCARBONS AND METHOD OF ISOMERIZATION OF AlCl3-ALKANE HYDROCARBONS

机译:C 4 -C 7 -烷烃的异构化催化剂和AlCl 3 -烷烃的异构化方法

摘要

FIELD: organic chemistry. SUBSTANCE: catalyst contains, mass % : Pt 0.129-0242, aluminium chloride having empirical formula AlCl3 5.5-5.8, aluminium oxide having empirical formula m as fire-proof carrier - the rest. Platinum is displaced in surface layer of catalyst, its surface concentration is at least 1.5 times that in control area of catalyst. Depth of surface layer is 150 C4-C7, diameter of central area being 50% of volume diameter of catalyst's particle. Isomerization of 5 h-1-alkane hydrocarbons is carried out at pressure 1-100 atm, temperature 40-250 is preferable. Molar ratio of hydrogen and hydrocarbons is (0.01-5): 1. Molar ratio of hydrogen and hydrocarbons in isomerization product is 0.05-: 1. It's preferable to conduct process in liquid-phase regime and to purify origin products against sulfur- and oxygen-containing compounds. Chlorocarbon is added into origin material as promoter, its quantity being 30-300 ppm. EFFECT: improves isomerization process. 8 cl, 1 dwg
机译:领域:有机化学。物质:催化剂含有质量%:Pt 0.129-0242,经验式为AlCl 3 5.5-5.8的氯化铝,经验式为m的氧化铝作为耐火载体。铂在催化剂表面层中位移,其表面浓度至少是催化剂控制区域中表面浓度的1.5倍。表面层的深度为150 C 4 -C 7 ,中心区域直径为催化剂颗粒体积直径的50%。 5 h Sup-1链烷烃的异构化是在1-100 atm的压力下进行的,优选40-250的温度。氢和碳氢化合物的摩尔比为(0.01-5):1.异构化产物中的氢和碳氢化合物的摩尔比为0.05-:1.最好在液相条件下进行工艺并纯化原始产物以对抗硫和氧含化合物。氯碳作为助催化剂加入到原料中,其量为30-300 ppm。效果:改善了异构化过程。 8厘升,1载重吨

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