首页> 外国专利> A method for the production of heavy metal bromine identical and, if necessary, hydrogen bromide from the destillationsrueckstand of the mother liquor after separation of the terephthalic acid in the case of the oxidation of p - dialkyl benz oils in flue polyethylene phase in the presence of heavy metal-containing, bromine activated oxidation catalysts and a lower aliphatic carbonsaeure resulting reaction mixture

A method for the production of heavy metal bromine identical and, if necessary, hydrogen bromide from the destillationsrueckstand of the mother liquor after separation of the terephthalic acid in the case of the oxidation of p - dialkyl benz oils in flue polyethylene phase in the presence of heavy metal-containing, bromine activated oxidation catalysts and a lower aliphatic carbonsaeure resulting reaction mixture

机译:在对苯二甲酸二烷基苯油在聚乙烯烟气中,在对苯二酚存在下氧化的情况下,分离对苯二甲酸后,从母液的蒸馏塔架上的蒸馏塔架上蒸馏出重金属溴的方法,必要时还可以从母液的蒸馏台上得到溴化氢。含重金属,溴活化的氧化催化剂和低级脂肪族碳酸钠生成的反应混合物

摘要

1460941 Catalyst recovery MATSUYAMA PETROCHEMICALS Inc 26 March 1974 [30 March 1973 26 April 1973] 13234/74 Heading C1A [Also in Division C2] Co, Mn and Br catalyst components are recovered in a pure form from the mother liquor residue of the oxidation of an alkylbenzene to terephthalic acid in a lower monocarboxylic acid after removal of said acid by (a) stirring the mother liquor residue with water and a sulphur compound chosen from H 2 S, Na 2 S, NaHS, KHS, NH 4 HS while blowing or compressing a molecular O 2 -containing gas into it, thereby extracting the catalyst components, (B) separating the solid impurities so formed, (C) passing the catalyst containing extract through a column packed with a strongly-acidic cation-exchange resin to absorb the Co and/or Mn, (D) distilling the eluate collected up to the point at which the Co and/or Mn begin to pass out of the bottom of the column, whereby bromine is recovered as HBr, (E) passing HBr solution through the column to desorb the Co and /or Mn, (F) distilling the eluate thus obtained to recover excess HBr and a solution of the Co and/or Mn bromides in a pure state. In a modification of the process, when cobalt is necessarily present, the addition of sulphide material in step A is omitted and a further step of diluting the aqueous extract from step 3 to give a Co concentration of less than 1 wt. per cent before continuing with step C is carried out.
机译:1460941催化剂回收松山石油化学株式会社1974年3月26日[1973年3月30日1973年4月26日] 13234/74标题C1A [也在C2部门中]以纯净的形式从氧化三氯甲烷的母液残渣中回收钴,锰和溴催化剂组分。 (a)将母液残余物与水和选自H 2 S,Na 2 S,NaHS,KHS,NH 4 HS的硫化合物在搅拌或搅拌下搅拌除去后,在低级一元羧酸中将烷基苯转化为对苯二甲酸。将含分子氧2的气体压缩到其中,从而萃取催化剂组分,(B)分离出如此形成的固体杂质,(C)使含催化剂的萃取物通过装有强酸性阳离子交换树脂的塔以吸收Co和/或Mn,(D)蒸馏收集的洗脱液直至Co和/或Mn开始从塔底流出,从而将溴作为HBr回收,(E)通过HBr溶液通过色谱柱解吸Co d.//Mn,(F)蒸馏如此获得的洗脱液以回收过量的HBr和纯状态的Co和/或Mn溴化物的溶液。在该方法的变型中,当必须存在钴时,省略了在步骤A中添加硫化物材料,并且进一步的步骤是稀释步骤3中的水提取物以得到小于1wt。%的Co浓度。继续执行步骤C之前,请先将百分比设置为%。

著录项

相似文献

  • 专利
  • 外文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号