IE43616B1 - A method of removing ozone from wate - Google Patents
A method of removing ozone from wateInfo
- Publication number
- IE43616B1 IE43616B1 IE181376A IE181376A IE43616B1 IE 43616 B1 IE43616 B1 IE 43616B1 IE 181376 A IE181376 A IE 181376A IE 181376 A IE181376 A IE 181376A IE 43616 B1 IE43616 B1 IE 43616B1
- Authority
- IE
- Ireland
- Prior art keywords
- water
- ozone
- coal
- granulated
- filter
- Prior art date
Links
Classifications
-
- 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
- C02F1/70—Treatment of water, waste water, or sewage by reduction
-
- 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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/42—Nature of the water, waste water, sewage or sludge to be treated from bathing facilities, e.g. swimming pools
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Filtering Materials (AREA)
Abstract
1532227 Ozone removal PATERSON CANDY INTERNATIONAL Ltd 12 Aug 1976 [22 Oct 1975] 43368/75 Heading C1C Ozone is removed from water by passing the ozonized water through a filter media which comprises granulated coal or a granulated synthetic polymeric material. The coal is preferably anthracite. Magnesite, marble or chalk pellets from a pellet softener may be added to the filter.
Description
The present invention relates to a method of removing ozone from water, particularly but not exclusively swimming pool water.
Both chlorine and ozone are effective disinfection agents, and are widely used in the treatment of water supplies and in swimming pools. Residual chlorine is relatively stable, particularly when combined with ammonia to form chloramine, whereas ozone decomposes on its own accord in about an hour.
Chlorine is very soluble in water and its concentration in air in- contact with the water is too low at normal disinfection levels to cause any hazard. On the other hand, ozone is far less soluble and is particularly toxic in air.
In a water treatment plant this is of little consequence because the ozone-decays in the early part of the distribution system and never reaches the consumer. However, if these agents are used in a swimming pool the time delay between purification and the return to the pool is very short indeed. Thus it is necessary to remove all the ozone prior to returning the wat
To maintain a residual sterilising action in the pool itself, it is desirable to maintain a residual level of chlorine, either free or combined, and if ozone is also used means are required for removing the ozone, preferably
-243616 without destroying the chlorine.
In a large pool installation, chlorine is usually supplied ar. a gas and therefore over a period it is necessary to add an alkali to maintain an acceptable pH value.
It has been known for many years that granulated activated carbon effectively destroys ozone as well as free and combined chlorine. Granulated activated carbon has also been used as a filter media. Unfortunately because it destroys chlorine, bacteria are able to breed within the pores of the carbon, and although the carbon may absorb certain impurities it is not uncommon for the filtered water to contain more bacteria than the incoming w-ter. In this case post chlorination is necessary.
The invention provides a method of removing ozone
1$ from water comprising the step of passing the ozonized water through a filter medium which comprises granulated coal or a granulated synthetic polymeric material.
Preferably the granulated coal or the granulated synthetic polymeric material is in the form of non-porous particles so that the particles may be cleaned by back-washing the filters. Preferably, the pH of the water is maintained at a required value by a suitable additive.
If so desired a medium such as crushed magnesite, marble or chalk pellets from a pellet softener may be added to
-33616 lhe i'il Ler.
By virtue of the high density of these materials they will fall to the bottom of the bed of anthracite, at which point the water will be clean and free from ozone.
Thus, hy way of example a purification system may include a sequence in which the raw water is passed down a packed column or a spray in a surrounding atmosphe>'e containing ozonized air. The ozonised water is then allowed to pass through a zone of sufficient volume to give the desired retention time for sterilisation or disinfection, and thence in through a filter media of sufficient size and depth both to remove suspended solids and to facilitate backwashing. 'x’his filter comprises anthracite, coal or a synthetic nonporous polymeric material. Finally, and optionally, the water would pass through a layer of pH correcting material and out through an underdrain system.
Any chlorine present in the incoming water would pass through unaffected.
The advantages of such a system over against granulated activated carbon or mixtures thereof with inert material are: (a) Avoidance of chlorine wastage and therefore lower operating costs.
(b) Lower initial and replacement costs of the filter media.
(c) Avoidance of bacterial contamination associated with activated carhon.
Claims (7)
1. A method of removing ozone from water comprising the step of passing the ozonized water through a niter medium which comprises granulated coal or a granulated synthetic polymeric material.
2. A method as claimed in claim 1 wherein the said coal is in the form of anthracite .
3. A method as claimed in claim 1 or claim 2, wherein the ganulated coal or the granulated synthetic polymeric material is in the form of non-porous particles so that the particles may be cleaned by back-washing the filter. I).. A method as claimed in claiin 2 or 3, wherein the pH of the water is maintained at a required value by a suitable additive.
4. 5. A method as claimed in claim 2, 3 or U> wherein magnesite, marble or chalk pellets from a pellet softener are added to the filter.
5. 6. A method for removing ozone from water according to any of claims 1 to 5 substantially as herein described with reference to the example given.
6.
7. Water in which the ozone has been removed by a method as claimed in any one of the preceding claims.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB4336875A GB1532227A (en) | 1975-10-22 | 1975-10-22 | Method of removing ozone from water |
Publications (2)
Publication Number | Publication Date |
---|---|
IE43616L IE43616L (en) | 1977-04-22 |
IE43616B1 true IE43616B1 (en) | 1981-04-08 |
Family
ID=10428470
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
IE181376A IE43616B1 (en) | 1975-10-22 | 1976-08-16 | A method of removing ozone from wate |
Country Status (2)
Country | Link |
---|---|
GB (1) | GB1532227A (en) |
IE (1) | IE43616B1 (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4425913A1 (en) * | 1994-07-21 | 1996-01-25 | Hoechst Ag | Methods and filters for removing organic matter and ozone from gases |
EP0697236A1 (en) * | 1994-08-15 | 1996-02-21 | Hoechst Aktiengesellschaft | Filter material and process for elimination of ozone from gases and liquides |
DE4429164A1 (en) * | 1994-08-17 | 1996-02-22 | Hoechst Ag | Filter material and process for removing ozone from gases and liquids |
DE4429165A1 (en) * | 1994-08-17 | 1996-02-22 | Hoechst Ag | Filter material and process for removing ozone from gases and liquids |
DE4431139A1 (en) * | 1994-09-01 | 1996-03-07 | Hoechst Ag | Process for eliminating ozone from gases and liquids |
KR100890246B1 (en) * | 2008-11-11 | 2009-03-24 | 서울특별시 | Upflow ozone contactor for quenching residual ozone |
-
1975
- 1975-10-22 GB GB4336875A patent/GB1532227A/en not_active Expired
-
1976
- 1976-08-16 IE IE181376A patent/IE43616B1/en unknown
Also Published As
Publication number | Publication date |
---|---|
IE43616L (en) | 1977-04-22 |
GB1532227A (en) | 1978-11-15 |
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