首页> 外国专利> CATALYST, SYNTHESIS METHOD THEREOF (VERSIONS) AND METHOD FOR LIQUID-PHASE ALKYLATION OF ISOBUTANE WITH C2-C4 OLEFINS IN PRESENCE SAID CATALYST

CATALYST, SYNTHESIS METHOD THEREOF (VERSIONS) AND METHOD FOR LIQUID-PHASE ALKYLATION OF ISOBUTANE WITH C2-C4 OLEFINS IN PRESENCE SAID CATALYST

机译:现行催化剂中C 2 -C 4 烯烃与异丁烷的液相烷基化催化剂,合成方法(版本)和方法

摘要

FIELD: chemistry.;SUBSTANCE: invention relates to petrochemistry, particularly to production of a zeolite-based catalyst for alkylation of isobutane with olefins and can be used in oil refining industry. Described is a zeolite-based catalyst for alkylation of isobutane with olefins which contains aluminium oxide and silicon dioxide with molar ratio of silicon dioxide to aluminium oxide equal to 2.8-7.0, sodium and rare-earth element oxides and active metal oxides in form of platinum oxide and/or palladium oxide and/or rhenium oxide and/or rhodium oxide and/or halogen - chlorine or fluorine, with the following ratio of components in wt %: sodium oxide 0.26-0.8, calcium oxide 0.8-4.2, rare-earth element oxide 12.1-20.0, platinum oxide and/or palladium oxide and/or rhenium oxide and/or rhodium oxide 0.02-2.0, and/or chlorine 0.05-0.8 and/or chlorine 0.005-0.5, a zeolite with ratio SiO2/Al2O3 equal to 2.8-7.0 being the balance. Disclosed also are two versions of the method of producing a zeolite-based catalyst for alkylation of isobutane with C2-C4 olefins, involving treatment thereof with aqueous solutions of salts of calcium, a rare-earth element and ammonium at high temperature and pressure of saturated vapour for a period of time necessary to convert the zeolite into a rare-earth calcium zeolite, and depositing active metal oxides onto it by saturation with aqueous solutions containing active metals, followed by washing, drying and calcination, where at the beginning, the obtained rare-earth calcium zeolite is saturated with unipolar water until the release of air from zeolite pores stops, and then depositing active metal oxides: platinum oxide and/or palladium oxide and/or rhenium oxide and/or rhodium oxide and/or halogen - chlorine or fluorine, taken in amounts which ensure said content of the oxide of the corresponding metal and halogen in the ready product, or deposition of active metal oxides - platinum oxide and/or palladium oxide and/or rhenium oxide and/or rhodium oxide and/or halogen - chlorine or fluorine - onto the rare-earth calcium zeolite is carried out from solutions containing the corresponding metals or halogen in unipolar water, taken in amounts which ensure said content of oxide of the oxide of the corresponding metal in the ready catalyst, wherein in both versions, deposition of active metals and halogen is carried out in two steps: at the first step via cold saturation at temperature not higher than 30°C for 1 hour, at the second step - at temperature not lower than 70°C for 1 hour, after which treatment with an organic acid is carried out in the presence of 30% aqueous hydrogen peroxide solution, followed by drying, tableting and calcination. Described is a method for liquid-phase alkylation of isobutane with olefins in the presence of the catalyst described above.;EFFECT: longer stable operation of the catalyst with activity thereof up to almost 100 wt % and isooctane selectivity of up to 75,7 wt %.;20 cl, 10 ex, 2 tbl
机译:技术领域本发明涉及石油化学,尤其涉及用于将异丁烷与烯烃烷基化的沸石基催化剂的生产,并且可用于炼油工业中。描述了一种用于异丁烷与烯烃的烷基化的沸石基催化剂,其包含氧化铝和二氧化硅,二氧化硅与氧化铝的摩尔比等于2.8-7.0,钠和稀土元素氧化物以及铂形式的活性金属氧化物氧化物和/或氧化钯和/或氧化rh和/或氧化铑和/或卤素-氯或氟,且以下成分的重量百分比比:氧化钠0.26-0.8,氧化钙0.8-4.2,稀土元素SiO 的分子氧化物12.120.0,氧化铂和/或氧化钯和/或氧化rh和/或氧化铑0.02-2.0,和/或氯0.05-0.8,和/或氯0.005-0.5 2 / Al 2 O 3 等于2.8-7.0。还公开了两种生产用于基于C 2 -C 4 的烯烃对异丁烷进行烷基化的沸石基催化剂的方法的方法,涉及用盐的水溶液处理该催化剂。钙,稀土元素和铵在高温和饱和蒸汽压力下保持一段时间,以将沸石转变成稀土钙沸石,并通过用含有活性金属的水溶液饱和而在其上沉积活性金属氧化物然后进行洗涤,干燥和煅烧,在开始时,将获得的稀土钙沸石用单极性水饱和,直到停止从沸石孔中释放空气,然后沉积活性金属氧化物:氧化铂和/或氧化钯和/或氧化rh和/或氧化铑和/或卤素-氯或氟,其添加量应确保成品中相应金属和卤素的氧化物的所述含量或活性物质的沉积金属氧化物-氧化铂和/或氧化钯和/或氧化铑和/或氧化铑和/或卤素-氯或氟-在稀土钙沸石上是从含有相应金属或卤素的单极性溶液中进行的水的量应确保在制备的催化剂中相应金属的氧化物的所述氧化物含量,其中在两种形式中,活性金属和卤素的沉积均分两个步骤进行:第一步是通过温度下的冷饱和在第二步骤中,在不高于30°C的温度下保持1小时-在不低于70°C的温度下保持1小时,此后在30%过氧化氢水溶液存在下用有机酸进行处理,然后干燥,压片和煅烧。描述了在上述催化剂存在下异丁烷与烯烃的液相烷基化的方法;效果:催化剂的更长的稳定运行,其活性高达几乎100wt%,异辛烷选择性高达75.7wt% %.; 20 cl,10 ex,2 tbl

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