GB751856A - Improvements in the recovery of acids from effluents using ion-exchange materials - Google Patents

Improvements in the recovery of acids from effluents using ion-exchange materials

Info

Publication number
GB751856A
GB751856A GB9419/53A GB941953A GB751856A GB 751856 A GB751856 A GB 751856A GB 9419/53 A GB9419/53 A GB 9419/53A GB 941953 A GB941953 A GB 941953A GB 751856 A GB751856 A GB 751856A
Authority
GB
United Kingdom
Prior art keywords
compartment
diaphragm
anion exchange
acid
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
GB9419/53A
Inventor
Thomas Victor Arden
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 GB9419/53A priority Critical patent/GB751856A/en
Publication of GB751856A publication Critical patent/GB751856A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/42Electrodialysis; Electro-osmosis ; Electro-ultrafiltration; Membrane capacitive deionization
    • B01D61/44Ion-selective electrodialysis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/42Electrodialysis; Electro-osmosis ; Electro-ultrafiltration; Membrane capacitive deionization
    • B01D61/422Electrodialysis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D65/00Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/02Membrane cleaning or sterilisation ; Membrane regeneration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J47/00Ion-exchange processes in general; Apparatus therefor
    • B01J47/12Ion-exchange processes in general; Apparatus therefor characterised by the use of ion-exchange material in the form of ribbons, filaments, fibres or sheets, e.g. membranes
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2321/00Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/16Use of chemical agents
    • B01D2321/168Use of other chemical agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/469Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/20Heavy metals or heavy metal compounds
    • C02F2101/22Chromium or chromium compounds, e.g. chromates

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Urology & Nephrology (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

751,856. Electrodialytic decomposition of salt solutions. PERMUTIT CO., Ltd. March 29, 1954 [April 7, 1953], No. 9419/53. Class 41. [Also in Group I] An aqueous effluent containing an acid is passed through an anion exchange material to take up the anions of the acid; these anions are removed in salt form from the anion exchange material during regeneration; and the salt is then electrolysed in a cell made up of two or more compartments separated from one another by one or more ion exchange diaphragms, to produce the acid. As shown, an effluent containing phosphoric acid is passed .through a bed of anion exchange material 3- the material being in the hydroxyl state-as shown by the dotted lines. Caustic soda is then passed through the bed to regenerate it and displace the phosphate anions taken up. The effluent regenerant is then electrolysed in the centre compartment 7 of a three compartment cell, the diaphragm 14 being a cation exchange diaphragm and the diaphragm 16 being an anion exchange diaphragm. Caustic soda is formed in the cathode compartment 4 and phosphoric acid in the anode compartment 5. Hydrogen and oxygen are liberated at the cathode and anode respectively. A two-compartment cell divided by an anion exchange or cation exchange diaphragm can also be used; in the former case the effluent regenerant is placed in the cathode compartment and in the latter case in the anode compartment for electrolysis. Specification 751,855 is referred to.
GB9419/53A 1953-04-07 1953-04-07 Improvements in the recovery of acids from effluents using ion-exchange materials Expired GB751856A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB9419/53A GB751856A (en) 1953-04-07 1953-04-07 Improvements in the recovery of acids from effluents using ion-exchange materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB9419/53A GB751856A (en) 1953-04-07 1953-04-07 Improvements in the recovery of acids from effluents using ion-exchange materials

Publications (1)

Publication Number Publication Date
GB751856A true GB751856A (en) 1956-07-04

Family

ID=9871611

Family Applications (1)

Application Number Title Priority Date Filing Date
GB9419/53A Expired GB751856A (en) 1953-04-07 1953-04-07 Improvements in the recovery of acids from effluents using ion-exchange materials

Country Status (1)

Country Link
GB (1) GB751856A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0041819A2 (en) * 1980-06-05 1981-12-16 Donald Weston Bolme Removal of nitrous material from nitric acid streams
NL9400504A (en) * 1994-03-30 1995-11-01 Elektrolyse Project B V Method for purifying a contaminated oxidizing solution in a dialysis cell
EP0701860A1 (en) * 1994-09-16 1996-03-20 LeaRonal, Inc. Electrolytic production of hypophosphorous acid
US5578182A (en) * 1994-09-16 1996-11-26 Learonal Inc. Electrolytic production of hypophosphorous acid

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0041819A2 (en) * 1980-06-05 1981-12-16 Donald Weston Bolme Removal of nitrous material from nitric acid streams
EP0041819A3 (en) * 1980-06-05 1982-07-14 Donald Weston Bolme Removal of nitrous material from nitric acid streams
NL9400504A (en) * 1994-03-30 1995-11-01 Elektrolyse Project B V Method for purifying a contaminated oxidizing solution in a dialysis cell
EP0701860A1 (en) * 1994-09-16 1996-03-20 LeaRonal, Inc. Electrolytic production of hypophosphorous acid
US5578182A (en) * 1994-09-16 1996-11-26 Learonal Inc. Electrolytic production of hypophosphorous acid

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