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XYLENE-CONTAINING NONEQUILIBRIUM FEED STOCK FLOW ISOMERISATION PROCEDURE

机译:含二甲苯的非平衡进料流的异构化程序

摘要

FIELD: chemistry.;SUBSTANCE: invention refers to xylene isomerisation in feed stock containing nonequilibrium mixture of two or more xylenes and optionally ethylbenzene characterised by that feed stock flow contacts with layered catalyst in catalytically effective amount in isomerisation environment including temperature within 100° to 550°C, absolute pressure within 10 kPa to 5 MPa and hydrogen to hydrocarbons molar ratio within 0.5:1 to 6:1, required for isomerisation product flow containing xylenes, where paraxylene takes at least 23 wt %, orthoxylene at least 21 wt %, and methaxylene at least 48 wt %. Said catalyst has an alpha-alumina frame of principal dimension at least 300 mcm coated with a layer of MFI molecular sieve structure with aperture diameter 4 to 8 angstrom, and an alumina or gamma-alumina binding material of thickness 250 mcm and less, and at least one hydrogenating metal component chosen of the group including Pt and Mo, as the binding material represents aluminium phosphate, and Re, as the binding material is represented by gamma-alumina. At least 75 wt % of hydrogenating metal component in the catalyst is accumulated in the layer wherein total amount of formed toluene and trimethylbenzene is 3 wt % and less of total xylenes and ethylbenzene in feed stock flow.;EFFECT: reduced loss of aromatic hydrocarbons and good balance approximation in isomerisation process.;7 cl, 4 tbl, 7 ex
机译:技术领域:本发明涉及包含两种或更多种二甲苯和任选的乙苯的非平衡混合物的原料中的二甲苯异构化,其特征在于,在包括温度在100°至550℃之间的异构化环境中,原料流以催化有效量与层状催化剂接触。 °C,绝对压力在10 kPa至5 MPa之内,氢与烃的摩尔比在0.5:1至6:1之内,这是对二甲苯异构化产物流的要求,其中对二甲苯占至少23 wt%,邻二甲苯占至少21 wt%,至少二甲亚甲基和48%(重量)。所述催化剂具有主要尺寸为至少300mcm的α-氧化铝框架,其涂覆有孔径为4至8埃的MFI分子筛结构层,以及厚度为250mcm或更小的氧化铝或γ-氧化铝粘结材料,且在从包括Pt和Mo的组中选择的至少一种氢化金属组分作为结合材料表示磷酸铝,以及作为结合材料的Re由γ-氧化铝表示。催化剂中至少有75 wt%的氢化金属成分积聚在该层中,其中形成的甲苯和三甲基苯的总量为原料流中二甲苯和乙苯总量的3 wt%以下;效果:减少了芳烃和异构化过程中良好的平衡近似。; 7 cl,4 tbl,7 ex

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