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CATALYST, METHOD FOR PRODUCING AND METHOD transalkylation of benzene with diethylbenzene with its use

机译:催化剂,生产方法和苯与二乙苯的烷基转移方法及其用途

摘要

FIELD: chemistry.;SUBSTANCE: invention relates to transalkylation catalysts. Described is a catalyst for transalkylation of benzene with diethylbenzenes in form of cylindrical granules with a regular shape, which contains zeolite Y in an acidic H+ form, which contains 100 wt % zeolite with degree of substitution of Na+ ions with H+ ions of not less than 0.95 and more than 80% of volume of the transported pores of the granules is made up of pores with diameter larger than 100 nm. Described is a method of producing said catalyst, which involves preparation of cylindrical granules with a regular shape, involving drying and calcination of the granules, wherein to obtain the catalyst, zeolite NaY, which is granulated with binding material and has high phase purity, wherein more than 80% of the volume of the transported pores is made up of pores with a diameter larger than 100 nm, is successively treated with aqueous solutions of ammonium salts with concentration of 20-25 g/dm3 (with respect to NH4+) with the ratio of mass of granules to volume of the solution of (1:6)-(1:7) and temperature of 80-90°C for 1.0-1.5 hours, alternating three or four steps of said treatment with two or three intermediate calcinations, respectively, at temperature of 540-600°C for 3-4 hours, drying at temperature of 120-150°C for 3-4 hours and calcining for 3-4 hours at temperature of 540-600°C. Described is a method for transalkylation of benzene with diethylbenzenes, involving reaction of benzene with diethylbenzenes in liquid phase at high temperature and pressure using said catalyst, wherein content of water in the material is less than 200 ppm.;EFFECT: high conversion of diethylbenzenes.;3 cl, 2 tbl, 10 ex
机译:烷基转移催化剂技术领域本发明涉及烷基转移催化剂。描述了一种用于以规则形状的圆柱形颗粒形式将苯与二乙苯进行烷基转移的催化剂,其包含呈酸性H + 形式的沸石Y,其包含100 wt%的Na取代度的沸石H + 离子不少于0.95且占颗粒传输孔体积的80%以上的 + 离子由直径大于100 nm的孔组成。描述了一种生产所述催化剂的方法,该方法包括制备具有规则形状的圆柱形颗粒,包括干燥和煅烧颗粒,其中为了获得催化剂,将沸石NaY与粘合材料一起制粒并且具有高相纯度,其中输送的孔中有80%以上是由直径大于100 nm的孔组成,并依次用浓度为20-25 g / dm 3 的铵盐水溶液处理(相对于NH 4 + ),颗粒质量与溶液体积的比为(1:6)-(1:7),温度为80 -90℃保持1.0-1.5小时,所述处理的三个或四个步骤分别与两次或三个中间煅烧交替进行,在540-600℃的温度下进行3-4小时,在120-150℃的温度下干燥3-4小时,并在540-600℃的温度下煅烧3-4小时。描述了一种使苯与二乙苯进行烷基转移的方法,包括使用所述催化剂在高温和高压下使苯与二乙苯在液相下反应,其中材料中的水含量小于200 ppm;效果:二乙苯的高转化率。 ; 3 cl,2 tbl,10前

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