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processes for the recovery of styrene and xylene from oil and new products obtained (craquee

机译:从石油和获得的新产品中回收苯乙烯和二甲苯的工艺

摘要

1,274,784. Extractive distillation; catalytic hydrogenation. TORAY INDUSTRIES Inc. 10 Feb., 1970 [17 Feb., 1969; 26 Aug., 1969], No. 6208/70. Heading C5E. Styrene and xylene are separated from hydrocarbon fractions by subjecting the fractions to extractive-distillation with a dialkylacetamide, dialkylsulphoxide, an alkylene carbonate, a lactone, phenol, m-cresol, aniline or an alkylaniline as solvent to obtain xylene in the distillate and styrene as a residue. The hydrocarbon fraction can be an oil produced in the thermal cracking of naphtha to ethylene and containing hydrocarbons having 5 to 9 carbon atoms. This oil can be distilled at atmospheric pressure in one or two separate columns to remove materials having up to 7 or more than 9 carbon atoms and the remaining material is passed to the extractive distillation. 10-500 p.p.m. of hydroquinone, t-butylcatechol, phenothiazine or sulphur can be included in the extractive distillation to inhibit polymerization of styrene. The extractive distillation can be carried out at below 120‹ C. and below 200 mm. Hg absolute with a reflux ratio between 10 and 30 in one column or in two columns. When two columns are used the extract solvent is fed to the tops of each column, the feed is passed to the middle of the first column and the bottoms from the first column is fed to the middle of the second column. The top fraction from the extractive distillation can be mixed with the up to C 7 material distilled from the feed and the mixture hydrogenated at 10-200 kg./sq. cm. abs. and 100- 400‹ C. using a catalyst of Co, Mo and/or W to produce ethylbenzene and o-, m- and p-xylenes.
机译:1,274,784。萃取蒸馏催化氢化。 TORAY INDUSTRIES Inc.,1970年2月10日[1969年2月17日; [1969年8月26日],第6208/70号。标题C5E。通过将馏分用二烷基乙酰胺,二烷基亚砜,碳酸亚烷基酯,内酯,苯酚,间甲酚,苯胺或烷基苯胺作为溶剂进行萃取蒸馏,从烃馏分中分离出苯乙烯和二甲苯,以在馏出物中获得二甲苯和苯乙烯。残留物。烃馏分可以是在石脑油热裂解成乙烯时产生的并且包含具有5至9个碳原子的烃的油。可以在大气压下在一个或两个单独的塔中蒸馏该油,以除去具有至多7个或9个以上碳原子的物质,并将剩余的物质送至萃取蒸馏。晚上10-500对苯二酚,叔丁基邻苯二酚,吩噻嗪或硫可以包括在萃取蒸馏中以抑制苯乙烯的聚合。萃取蒸馏可以在低于120℃和低于200mm下进行。绝对汞含量,一栏或两栏的回流比在10到30之间。当使用两塔时,将萃取溶剂进料到每塔的顶部,进料被送到第一塔的中间,而第一塔的塔底被进料到第二塔的中间。可以将萃取蒸馏的塔顶馏分与进料中蒸馏出的最高C 7物料混合,并将混合物以10-200 kg./sq的压力氢化。厘米。腹肌在100-400℃下使用Co,Mo和/或W的催化剂生产乙苯和邻,间和对二甲苯。

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