GB902347A - Improvements relating to the ion-exchange treatment of water - Google Patents
Improvements relating to the ion-exchange treatment of waterInfo
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J47/00—Ion-exchange processes in general; Apparatus therefor
- B01J47/02—Column or bed processes
- B01J47/04—Mixed-bed processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Treatment Of Water By Ion Exchange (AREA)
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.
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)
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 |
-
1959
- 1959-04-20 GB GB1341659A patent/GB902347A/en not_active Expired
Cited By (7)
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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