GB902347A - Improvements relating to the ion-exchange treatment of water - Google Patents

Improvements relating to the ion-exchange treatment of water

Info

Publication number
GB902347A
GB902347A GB1341659A GB1341659A GB902347A GB 902347 A GB902347 A GB 902347A GB 1341659 A GB1341659 A GB 1341659A GB 1341659 A GB1341659 A GB 1341659A GB 902347 A GB902347 A GB 902347A
Authority
GB
United Kingdom
Prior art keywords
vessel
pipe
valve
layer
water
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
GB1341659A
Inventor
Frank Charles Blight
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 GB1341659A priority Critical patent/GB902347A/en
Publication of GB902347A publication Critical patent/GB902347A/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
    • B01J47/00Ion-exchange processes in general; Apparatus therefor
    • B01J47/02Column or bed processes
    • B01J47/04Mixed-bed processes
    • 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
    • C02F1/42Treatment of water, waste water, or sewage by ion-exchange

Abstract

902,347. Ion-exchange. PERMUTIT CO. Ltd. April 14, 1960 [April 20, 1959], No. 13416/59. Class 46. When water is being treated for the removal of dissolved salts, it enters the vessel 2 through a pipe 7 and leaves through the device 6. When regeneration is required the mixed bed, and the top layer 3 of cation-exchange material, is washed by upward flow of water from a pipe 13, this water flowing to waste through a pipe 14. The valves 8 and 11 are then shut and the materials are allowed to stratify into layers 15 and 16 as shown in Fig. 2, all the cationexchange material forming the bottom layer 16. Next a volume of material equal to that of the layer 3 is moved into a vessel 21, which acts as a measuring vessel; valves 17 and 18 are opened and water flows under pressure through the opened valve 17 into the vessel, and carries with it enough material to form a bed 22, (not shown), in vessel 21. The valves 17 and 18 are then shut again; the layers 15 and 16 move downwards and regeneration of the materials now takes place in the usual way, an alkali being introduced from a source 25 and passing out through the device 5. When the layer 15 has been regenerated the valve 8 is shut, the valve 10 is opened to connect the pipe 9 to a pipe 27, and the valve 11 is set to connect a source 47 of acid or brine to the pipe 12. The acid flows downwards through the layer 16 in the vessel 2 and then through the pipe 27 to the device 28 in the vessel 21, and thence through the material that has been moved into this vessel. The effluent acid regenerant flows to waste through the device 23 and pipe 24. At the end of this step the valve 11 is set to allow water to flow from a pipe 48 through the layer 16 in the vessel 2 and then through the material in the vessel 21 to rinse away excess regenerant. Next the valves 11 and 10 and a valve 29 in the pipe 24 are shut, and the layers 15, 16 are formed into a fresh mixed bed 1 by the upward flow of compressed air introduced through the valve 10 and device 6 and escaping through the pipe 34. Then the valve 18 is set to connect a pipe 30 to the vessel 21, while a valve 31 in a pipe 32 at the bottom of the vessel is opened. Water under pressure flows through the pipe 30 into the vessel 21 and carries the cationexchange material 22 through the pipe 32 back to the vessel 2 to form a new layer 3. The process may also be modified in that the device 5 may be at a higher point in the main vessel 2, that is to say at the level of the top of the cation-exchange layer. In such a case there is no regeneration outside the vessel 1 at all, and the bottom layer of regenerated cationexchange material is moved from the vessel 2, to the vessel 21 only to allow remixing to take place and is immediately thereafter returned to the vessel 2 to form the top layer 3. The vessel 21 therefore needs no device 28. A process in which the regeneration takes place outside the vessel in which the water is treated is also described. A second vessel of substantially the same size as the vessel 2 is provided instead of the vessel 21.
GB1341659A 1959-04-20 1959-04-20 Improvements relating to the ion-exchange treatment of water Expired GB902347A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB1341659A GB902347A (en) 1959-04-20 1959-04-20 Improvements relating to the ion-exchange treatment of water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1341659A GB902347A (en) 1959-04-20 1959-04-20 Improvements relating to the ion-exchange treatment of water

Publications (1)

Publication Number Publication Date
GB902347A true GB902347A (en) 1962-08-01

Family

ID=10022564

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1341659A Expired GB902347A (en) 1959-04-20 1959-04-20 Improvements relating to the ion-exchange treatment of water

Country Status (1)

Country Link
GB (1) GB902347A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0428868A2 (en) * 1989-10-20 1991-05-29 Ebara Corporation Materials for removing suspended impurities
EP0487455A1 (en) * 1990-11-19 1992-05-27 Christ AG Process and apparatus for desalinization of aqueous liquids
EP0502629A1 (en) * 1991-02-20 1992-09-09 Rohm And Haas Company Process of removing from water suspended metal corrosion products insoluble or sparingly soluble in water
BE1005513A5 (en) * 1991-10-11 1993-08-31 Ecowater Systems Inc Water softener.
US5308876A (en) * 1989-10-20 1994-05-03 Ebara Corporation Materials for removing suspended impurities and use thereof

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0428868A2 (en) * 1989-10-20 1991-05-29 Ebara Corporation Materials for removing suspended impurities
EP0428868A3 (en) * 1989-10-20 1991-09-18 Ebara Corporation Materials for removing suspended impurities and use thereof
US5308876A (en) * 1989-10-20 1994-05-03 Ebara Corporation Materials for removing suspended impurities and use thereof
EP0487455A1 (en) * 1990-11-19 1992-05-27 Christ AG Process and apparatus for desalinization of aqueous liquids
EP0502629A1 (en) * 1991-02-20 1992-09-09 Rohm And Haas Company Process of removing from water suspended metal corrosion products insoluble or sparingly soluble in water
BE1005513A5 (en) * 1991-10-11 1993-08-31 Ecowater Systems Inc Water softener.
US5464532A (en) * 1991-10-11 1995-11-07 Ecowater Systems, Inc. Water softener with resin beads of different mesh sizes

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