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A method for the purification of naphthalene by selective hydrogenation and subsequent separation

机译:一种通过选择性加氢和后续分离提纯萘的方法

摘要

The invention relates to a process for the purification of naphthalene. This process comprises a selective hydrotreatment corresponding to a hydrodesulphurization and / or hydrodenitrogenation and / or hydrodéhydroxylation and / or hydrogenation of olefins, while limiting the hydrogenation of the naphthalene. The catalyst used comprises a matrix, at least one metal of group viii, at least one metal from group vi and optionally phosphorous. It has a specific surface area of at most of 220 m * * 2 / g, a pore volume of 0,35 - 0,7 ml / g and an average pore diameter of more than 10 nm. The process carried out at 150 - 325 deg.c, under 0,1 - 0,9 mpa, with an hsv of 0,05 - 10h * * - 1, a ratio h2 / naphthalene of 0,1 - 1,3 mol / mol. The effluent from h2 s, nh3 and the water is subjected to a method of separation of the naphthalene by distillation or preferably by crystallization. In addition, a recycling of tetralin separated to the hydrotreatment makes it possible to significantly increase the yield of naphthalene. In this case, the weight ratio of tetralin / naphthalene to the input of the reactor is between 0,005 and 0,08.par.
机译:本发明涉及一种萘的纯化方法。该方法包括对应于烯烃的加氢脱硫和/或加氢脱氮和/或加氢二羟化和/或加氢的选择性加氢处理,同时限制了萘的氢化。所用的催化剂包括基质,至少一种第vi族的金属,至少一种第vi族的金属和任选的磷。其比表面积最大为220m * * 2 / g,孔体积为0.35-0.7ml / g,平均孔径大于10nm。该方法在150-325℃,0.1-0.9 MPa下,hsv为0.05-10h * *-1,h2 /萘比为0.1-1,3 mol的条件下进行/摩尔来自h 2 s,nh 3和水的流出物经过蒸馏或优选通过结晶分离萘的方法。另外,将分离的四氢萘酚再循环至加氢处理使得可以显着提高萘的收率。在这种情况下,四氢化萘/萘与反应器入口的重量比为0.005至0.08par。

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