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    • 6. 发明公开
    • Method of using higher concentration sulfuric acid for stripping and precipitation of adsorbed magnesium
    • 使用硫酸在更高的浓度,以拔出的方法和adsorbierdem镁的情况下。
    • EP0068413A2
    • 1983-01-05
    • EP82105467.3
    • 1982-06-22
    • AMERICAN PETRO MART, INC.
    • Hedrick, Harold NelsonWhitney, Solon Gene
    • B01J49/00C22B3/00
    • C01F5/40B01J49/12B01J49/53C22B3/24C22B3/42Y02P10/234
    • 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.
    • 吸附的镁从由洗脱阳离子交换树脂与20〜70%的硫酸作为负载的树脂的增量移动向上在汽提塔中,在该塔的顶部和降低浓度的硫酸与正被去除的再生树脂除去 洗脱的镁从塔的下部取出。 该硫酸浓度进行控制,以便做的再生溶液可以从硫酸的商业浓度来形成而没有不适当的稀释,所以没有镁可以从所述洗提液通过不添加大量的商业浓度酸的增加硫酸浓度沉淀 , 作为废料产生的稀硫酸的量保持在最低限度,而主要硫酸副产物具有有效高浓度,颜色:例如可用于治疗磷矿石。
    • 9. 发明公开
    • Method of using higher concentration sulfuric acid for stripping and precipitation of adsorbed magnesium
    • 使用较高浓度硫酸浸渍和降解吸附镁的方法
    • EP0068413A3
    • 1983-05-04
    • EP82105467
    • 1982-06-22
    • AMERICAN PETRO MART, INC.
    • Hedrick, Harold NelsonWhitney, Solon Gene
    • B01J49/00C22B03/00
    • C01F5/40B01J49/12B01J49/53C22B3/24C22B3/42Y02P10/234
    • 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.
    • 通过用20至70%的硫酸溶液从阳离子交换树脂中除去吸附的镁,随着负载树脂的增量在汽提塔中向上移动,再生树脂在柱顶部除去,浓缩的硫酸浓度降低 洗脱的镁从柱的下部除去。 控制硫酸浓度,使得再生溶液可以从商业浓度的硫酸形成而没有不适当的稀释,并且通过增加硫酸浓度而不添加大量的商业浓度的酸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,而主要的硫酸副产物具有有效的高浓度,例如可用于处理磷酸盐岩。