首页> 外国专利> METHOD OF CATION EXCHANGE RESIN REGENERATION USING HIGHER CONCENTRATION OF SULFURIC ACID FOR STRIPPING AND PRECIPITATING ADSORBED MAGNESIUM

METHOD OF CATION EXCHANGE RESIN REGENERATION USING HIGHER CONCENTRATION OF SULFURIC ACID FOR STRIPPING AND PRECIPITATING ADSORBED MAGNESIUM

机译:更高浓度的硫酸用于剥离和沉淀吸附镁的阳离子交换树脂的再生方法

摘要

Adsorbed magnesium is removed from a cation exchange resin by elution with 20 to 70% sulfuric acid as increments of the loaded resin move upwardly in a stripping column, the regenerated resin being removed at the top of the column and the sulfuric acid of reduced concentration with the eluted magnesium is removed from the lower portion of the column. The sulfuric acid concentrations are controlled so that the regenerating solution can be formed from commercial concentrations of sulfuric acid without undue dilution, and so that magnesium can be precipitated from the eluting solution by increasing the sulfuric acid concentration without adding a large amount of commercial concentration acid. The amount of dilute sulfuric acid produced as a waste material is kept to a minimum, while the principal sulfuric acid by-produkt has a usefully high concentration, such as may be employed for treatment of phosphate rock.
机译:在汽提塔中,随着负载树脂的增量向上移动,通过用20%至70%的硫酸洗脱,从阳离子交换树脂中去除吸附的镁,再生的树脂在塔的顶部被去除,而浓度较低的硫酸被去除。洗脱的镁从塔的下部除去。控制硫酸的浓度,以使再生溶液可以由商业浓度的硫酸形成而无需过度稀释,并且通过增加硫酸浓度而无需添加大量商业浓度的酸就可以从洗脱溶液中沉淀出镁。 。作为废料生产的稀硫酸的量保持最小,而主要的副产物硫酸具有有用的高浓度,例如可用于处理磷矿石。

著录项

  • 公开/公告号PT75080B

    专利类型

  • 公开/公告日1984-05-09

    原文格式PDF

  • 申请/专利权人 AMERICAN PETRO MART INC.;

    申请/专利号PT19820075080

  • 发明设计人

    申请日1982-06-18

  • 分类号B01J49/00;

  • 国家 PT

  • 入库时间 2022-08-22 09:14:00

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