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    • 3. 发明授权
    • Regeneration of thiocyanate resins
    • 硫氰酸酯树脂的再生
    • US4608176A
    • 1986-08-26
    • US683131
    • 1984-12-18
    • Christopher A. Fleming
    • Christopher A. Fleming
    • B01J49/00
    • B01J49/0013B01J49/0073
    • A method of regenerating strong-base anion exchange resins which have been used in the extraction of complex anions followed by elution with a thiocyanate strip solution is provided. The method involves the use of ferric ions in a regenerating solution together with a substitute anion for attachment of the resin, the regeneration taking place under conditions in which ferric-thiocyanate complex cations are formed and washed from the resin by the regenerating solution. The thiocyanate can be recovered by neutralizing the regenerating solution to precipitate ferric hydroxide and leave thiocyanate in solution.
    • 提供了已经用于萃取络合物阴离子然后用硫氰酸盐条溶液洗脱的强碱性阴离子交换树脂的再生方法。 该方法包括在再生溶液中使用三价铁离子与替代阴离子一起用于树脂的附着,再生在其中形成硫氰酸铁络合物阳离子并通过再生溶液从树脂中洗涤的条件下进行。 可以通过中和再生溶液沉淀氢氧化铁并将硫氰酸盐溶解在溶液中来回收硫氰酸盐。
    • 5. 再颁专利
    • Regeneration of anion exchange resins
    • 阴离子交换树脂的再生
    • USRE29680E
    • 1978-06-27
    • US310383
    • 1972-11-29
    • Eli SalemDonald J. ButterworthLeo F. Ryan
    • Eli SalemDonald J. ButterworthLeo F. Ryan
    • B01D15/04B01J49/00
    • B01J49/0013
    • The invention relates to a method for converting strong-base anion exchange resins from the monovalent anion form to the hydroxide form. A .�.solution.!. .Iadd.source .Iaddend.of polyvalent anions is first passed through the resin to displace the monovalent anions. A solution of alkali metal hydroxide is then passed through the resin to convert it to the hydroxide form, and to produce an effluent solution of hydroxide ions and polyvalent anions. This effluent solution is then neutralized with an acid containing .Iadd.a source of .Iaddend.polyvalent anions, and the neutralized solution is passed through a second batch of resin in the monovalent anion form. In the preferred embodiment, a portion of the effluent is retained without neutralization and is delivered to the second batch of resin after the neutralized effluent to perform a portion of the hydroxide regeneration.
    • 1339788转换阴离子交换树脂ECODYNE CORP 1971年4月19日[1970年4月20日] 26264/71标题C3P [也在B1部分具有季铵活性基团的强碱阴离子交换树脂从一价阴离子形式(氢氧化物除外)转化为 氢氧化物形式通过使多价阴离子的水源通过第一批树脂以用多价阴离子从树脂中取代一价阴离子; 随后将碱金属氢氧化物水溶液通过树脂将树脂转化为氢氧化物形式,并制备含有氢氧根阴离子和多价阴离子的含水流出物溶液; 用含有多价阴离子源的酸中和至少一部分流出物溶液以形成中和的多价阴离子源; 并使中和源以一价阴离子形式通过第二批树脂以从其中置换一价阴离子。 “一价阴离子形式”是指氢氧化物形式以外的树脂形式。 “中和源”仅比排出液更酸性,并且可以是酸性,中性或甚至碱性。 合适的树脂是通过使叔胺与单乙烯基芳族烃和二乙烯基芳族烃的卤代甲基化交联共聚物反应而制备的树脂, 苯乙烯和二乙烯基苯的共聚物与或不与乙基乙烯基苯。 其它合适的树脂是叔胺与卤代烷基化,优选氯甲基化的乙烯基芳族化合物的共聚物的反应产物,例如乙烯基芳族化合物。 苯乙烯或乙烯基茴香醚和少量的聚烯烃化合物,例如, 二乙烯基苯,异戊二烯,丁二烯或三乙烯基苯。 在该实施例中使用氢氧化钠,硫酸钠和硫酸。
    • 7. 发明授权
    • Method of ion exchange
    • 离子交换方法
    • US5084185A
    • 1992-01-28
    • US377582
    • 1989-07-10
    • George S. SoltAndrzej W. Nowosielski-Slepowron
    • George S. SoltAndrzej W. Nowosielski-Slepowron
    • B01J41/04B01J49/00
    • B01J41/043B01J49/0013Y10S210/903
    • The present invention relates to a method of reducing the concentration of contaminant ions, preferably nitrates ions, in impure water. The method comprises steps of: a) passing the impure water through an ion exchange resin to substitute regenerant ions from the resin for dissolved contaminant ions; b) passing a relatively dilute aqueous solution of wash-out ions through said resin to substitute wash-out ions for contaminant ions bound to the resin and; c) passing a relatively concentrated aqueous solution of regenerant ions through said resin to substitute regenerant ions for wash-out ions bound to the resin. The affinity of the resin to wash-out ions diminishes from being greater than that for contaminant and regenerant ions when exposed to a relatively dilute ionic solution to being less than that for said contaminant and regenerant ions when exposed to a relatively concentrated ionic solution. The method allows simplified ion exchange apparatus to be utilized, since the raw water, wash-out solution and regenerant solution may all be passed through the ion exchange resin in the same direction.
    • 本发明涉及在不纯的水中降低污染物离子(优选硝酸根离子)的浓度的方法。 该方法包括以下步骤:a)使不纯的水通过离子交换树脂以代替来自树脂的再生剂离子用于溶解的污染物离子; b)将相对稀释的洗出的离子水溶液通过所述树脂,以将洗出的离子替换为与树脂结合的污染物离子; c)使相对浓缩的再生剂离子水溶液通过所述树脂,以代替再生剂离子以与树脂结合的洗出离子。 当暴露于相对浓缩的离子溶液时,当暴露于相对稀释的离子溶液时,树脂对洗涤离子的亲和力比大于污染物和再生离子的亲和力降低到小于所述污染物和再生离子的亲和力。 该方法允许使用简单的离子交换装置,因为原水,洗出溶液和再生剂溶液都可以沿相同方向通过离子交换树脂。
    • 8. 发明授权
    • Cyanide recovery
    • 氰化物恢复
    • US4267159A
    • 1981-05-12
    • US176355
    • 1980-08-08
    • George J. Crits
    • George J. Crits
    • B01J41/04B01J49/00C01C3/08C02F1/42C22B3/00
    • B01J41/043B01J49/0013C01C3/08C22B3/42Y02P10/234Y10S210/904
    • Spent aqueous liquor containing cyanide, as from ore treatment, is passed through a bed of suitable anion-exchange resin to segregate the cyanide, which is subsequently recovered in regeneration of the resin by weak alkaline solution. Both the eluted cyanide and the alkaline regenerant are recycled, if desired, for further ore treatment. A most important benefit of such procedure is nearly complete elimination of cyanide as a component of the treatment effluent. Free cyanide may be separated from complexed cyanides when present by using weak alkaline regenerant to elute the free cyanide from the resin and stronger alkaline regenerant to elute the complexed cyanides.
    • 含有氰化物的废液从矿石处理通过合适的阴离子交换树脂床,以分离出氰化物,氰化物随后通过弱碱性溶液在树脂再生中回收。 如果需要,洗脱的氰化物和碱性再生剂都被再循环用于进一步的矿石处理。 这种方法的最重要的益处是几乎完全消除作为处理流出物的组分的氰化物。 通过使用弱碱性再生剂,游离氰化物可以从络合的氰化物中分离出来,以从树脂中洗脱游离氰化物和更强碱性再生剂以洗脱络合的氰化物。