GB630979A - Improvements in or relating to the recovery of salts from dilute solution - Google Patents

Improvements in or relating to the recovery of salts from dilute solution

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Publication number
GB630979A
GB630979A GB3384346A GB3384346A GB630979A GB 630979 A GB630979 A GB 630979A GB 3384346 A GB3384346 A GB 3384346A GB 3384346 A GB3384346 A GB 3384346A GB 630979 A GB630979 A GB 630979A
Authority
GB
United Kingdom
Prior art keywords
solution
acid
salt
hydrogen
passed
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB3384346A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Permutit Co Ltd
Original Assignee
Permutit Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Permutit Co Ltd filed Critical Permutit Co Ltd
Priority to GB3384346A priority Critical patent/GB630979A/en
Publication of GB630979A publication Critical patent/GB630979A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J39/00Cation exchange; Use of material as cation exchangers; Treatment of material for improving the cation exchange properties

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Treatment Of Water By Ion Exchange (AREA)

Abstract

In obtaining a relatively concentrated solution of a salt of a strong acid from a relatively dilute solution of the same salt or another salt having the same cation, the dilute solution is passed through hydrogen-ion-exchange material, a solution of the acid of which the salt is to be obtained is passed through the material, more acid is added to the effluent and the resultant solution is passed through one or more beds of hydrogen-ion-exchange material which have taken up cations from the initial solution, the last two steps being repeated if desired. In one embodiment the dilute solution is passed through a number of beds of exchange material in series followed by the acid solution, the initial concentration of which is restored during its passage between each bed and the next by the addition of acid; in a modification the regeneration may be effected with two different portions of acid solution, the acid concentration of each being restored after each passage through a bed and the second solution being used again as the first solution in a subsequent process after the beds have been again treated with the dilute salt solution. The material used for removal of the displacing acid from the final effluent may be one which will not exchange hydrogen for metal ions in solution with strong acid anions but will do so when these are in solution with weak acid anions. A similar material may be used for an initial solution which contains the salt of a weak acid, and for an initial solution which contains a mixture of salts of strong and weak acids, e.g. potassium sulphate and acetate; while this material is being saturated the effluent contains unchanged potassium sulphate which can be absorbed by material capable of exchanging for hydrogen ions the potassium ions from salts of strong acids, e.g. a cation exchange material having replaceable hydrogen ions forming part of sulphonic acid groups; the saturated material on regeneration results in a solution containing potassium sulphate and free sulphuric acid from which the latter may be removed by passage through exchange material already saturated with potassium ions or by neutralization with potassium hydroxide or carbonate.ALSO:In obtaining a relatively concentrated solution of a salt of a strong acid from a relatively dilute solution of the same salt or another salt having the same cation, the dilute solution is passed through hydrogen-ion-exchange material, a solution of the acid of which the salt is to be obtained is passed through the material, more acid is added to the effluent and the resultant solution is passed through one or more beds of hydrogen-ion-exchange material which have taken up cations from the initial solution, the last two steps being repeated if desired. In one embodiment the dilute solution is passed through a number of beds of exchange material in series followed by the acid solution, the initial concentration of which is restored during its passage between each bed and the next by addition of acid; in a modification the regeneration may be effected with two different portions of acid solution, the acid concentration of each being restored after each passage through a bed and the second solution being used again as the first solution in a subsequent process and the second solution being used again with dilute salt solution. The material used for removal of the displacing acid from the final effluent may be one which will not exchange hydrogen for metal ions in solution with strong acid anions but will do so when these are in solution with weak acid anions. A similar material may be used for an initial solution which contains the salt of a weak acid and for an initial solution which contains a mixture of salts of strong and weak acids, e.g., potassium sulphate and acetate; while this material is being saturated, the effluent contains unchanged potassium sulphate which can be absorbed by material capable of exchanging for hydrogen ions the potassium ions from salts and strong acids, e.g., a cation exchange material having replaceable hydrogen ions forming part of sulphonic acid groups; the saturated material on regeneration results in a solution containing potassium sulphate and free sulphonic acid from which the latter may be removed by passage through exchange material already saturated with potassium ions or by neutralization with potassium hydroxide or carbonate.
GB3384346A 1946-11-19 1946-11-19 Improvements in or relating to the recovery of salts from dilute solution Expired GB630979A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB3384346A GB630979A (en) 1946-11-19 1946-11-19 Improvements in or relating to the recovery of salts from dilute solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB3384346A GB630979A (en) 1946-11-19 1946-11-19 Improvements in or relating to the recovery of salts from dilute solution

Publications (1)

Publication Number Publication Date
GB630979A true GB630979A (en) 1949-10-25

Family

ID=10358163

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3384346A Expired GB630979A (en) 1946-11-19 1946-11-19 Improvements in or relating to the recovery of salts from dilute solution

Country Status (1)

Country Link
GB (1) GB630979A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3096153A (en) * 1960-10-17 1963-07-02 Standard Magnesium Corp Inc Ion exchange process for producing potassium sulfate and sulfuric acid

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3096153A (en) * 1960-10-17 1963-07-02 Standard Magnesium Corp Inc Ion exchange process for producing potassium sulfate and sulfuric acid

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