WO1995019937A1 - Plant that purifies water from iron and manganese by aeration and filtration - Google Patents
Plant that purifies water from iron and manganese by aeration and filtration Download PDFInfo
- Publication number
- WO1995019937A1 WO1995019937A1 PCT/SE1995/000071 SE9500071W WO9519937A1 WO 1995019937 A1 WO1995019937 A1 WO 1995019937A1 SE 9500071 W SE9500071 W SE 9500071W WO 9519937 A1 WO9519937 A1 WO 9519937A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- tank
- water
- filter
- level
- pump
- 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.)
- Ceased
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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/74—Treatment of water, waste water, or sewage by oxidation with air
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/02—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration
- B01D24/10—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration the filtering material being held in a closed container
- B01D24/12—Downward filtration, the filtering material being supported by pervious surfaces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/46—Regenerating the filtering material in the filter
- B01D24/4631—Counter-current flushing, e.g. by air
- B01D24/4642—Counter-current flushing, e.g. by air with valves, e.g. rotating valves
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/48—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof integrally combined with devices for controlling the filtration
- B01D24/4869—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof integrally combined with devices for controlling the filtration by level measuring
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/48—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof integrally combined with devices for controlling the filtration
- B01D24/4884—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof integrally combined with devices for controlling the filtration by pressure measuring
-
- 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
- C02F1/58—Treatment of water, waste water, or sewage by removing specified dissolved compounds
- C02F1/62—Heavy metal compounds
- C02F1/64—Heavy metal compounds of iron or manganese
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2201/00—Details relating to filtering apparatus
- B01D2201/18—Filters characterised by the openings or pores
- B01D2201/188—Multiple filtering elements having filtering areas of different size
Definitions
- This invention relates to a water treatment device or plant comprising a treatment tank under atmospheric pressure, a first pump for level-operated supply of raw water to the tank, a means for feeding a mixture of air and raw water to the upper part of the treatment tank, a filter disposed in the tank on a lower level than the feeding means, a collecting magazine for treated water disposed below the filter, a pressure tank connected to the collecting magazine, and a filter-washing device.
- a water treatment plant it is essential that the consumer continuously has access to water, regardless of the current phase of the water treatment process.
- the treatment process may be divided into four phases:
- the water from bored wells contains iron and/or manganese compounds that have to be removed before the water can be used in the household.
- air is usually admixed to the water, such that the iron and/or manganese compounds form insoluble oxides that can be disposed of by precipitation or filtering.
- the filter employed have to be regenerated at times, i.e. be backwashed with clean water.
- backwashing involves such a considerable consumption of water as to be impracticable in plants with small water resources. If so, one has to content oneself with preci ⁇ pitating the oxides and flushing out the resulting preci ⁇ pitate.'
- FI-78143 discloses a water treatment plant for self- contained houses, which enables a regeneration of the filter.
- This plant has the disadvantage of a low capacity due to the fact that the replenishment phase and the transfer phase cannot occur at the same time, one and the same pump being used in both phases.
- Another disadvantage is that the oily film of precipitates which are lighter than water and thus accumulate on the water surface in the tank during operation is not removed by the regenera ⁇ tion process. These precipitates often contain iron and manganese. When the water level has sunk to the level of the outlet connected to the upper surface of the filter, the outlet begins to draw air and no longer draws any water, leaving the oily film in the tank.
- the main object of the invention is to obviate the inconveniences of the prior-art water treatment plant described above.
- Another object of the invention is to make the effi ⁇ ciency of the backwashing phase independent of the amount of water found in the upper part of the tank when the filter is being backwashed. According to the invention, these objects are attained by a water treatment plant being of the type stated by way of introduction and having the distinctive features recited in the characterising clauses of the appended claims. The invention will be described in more detail below with reference to the accompanying drawing, which schema ⁇ tically illustrates a water treatment plant according to the invention.
- the drawing shows an essentially cylindrical tank 1 provided with a lid 2, which carries an ejector 3 for admixing air to raw water supplied through a conduit 4.
- the design of the ejector 3 is described in Swedish Patent Application 9303412-2.
- Water from a source 5 is supplied to the conduit 4 by a first pump 7 driven by a motor 6. Further, the motor 6 is controlled by a relay 8, to which are connected vertical electrodes 9, 10 and 11 of different lengths, which are arranged in the tank 1.
- An overflow 31 is arranged in the tank 1 on a level above the end of the shortest electrode 9.
- a sand fil ⁇ ter 13 on a level below the longest electrode 11.
- the filter 13 contains different-sized particles, the size of which increases in the direction of the lower part of the filter. Also, the filter 13 rests on a horizontal grating 14 mounted in the tank 1.
- a conduit 16 connecting the magazine 15 to a pressure tank 17 is provided with a second pump 18, which is driven by a motor 19 that in known manner is controlled by the pressure in the pressure tank, as well as with a non- return valve 20.
- a conduit 21 serves to conduct water from the pres ⁇ sure tank 17 to a place of consumption.
- a control system 24 with a timer is adapted to periodically deactivate the pump 18 while at the same time opening the solenoid valve 23.
- a siphon 30 In combination with the overflow 31 mentioned above, there is provided a siphon 30, whose open end is located at a distance from the upper surface of the filter which it faces.
- the siphon which consists of an inverted U-pipe, has one leg connected to the one horizontal arm of the overflow, which consists of an inverted T-pipe, whose other arm is connected, via a hole in the tank wall, to an outlet tube 32 leading to an outlet 33.
- the body of the T extends vertically upwards, ending slightly above the curve of the U-pipe.
- the legs of the U-pipe have different diameters.
- the leg whose opening is adjacent to the filter has a larger diameter than the other leg.
- the former leg has a diameter of 40 mm, whereas the latter leg has a diameter of 25 mm. This serves to increase the suction capacity of the siphon.
- the water treatment plant shown in the drawing and described above operates as follows.
- the motor 6 of the first pump 7 is activated by the relay 8.
- raw water from the source 5 is supplied through the conduit 4 to the ejector 3, where it is mixed with air drawn into the ejector 3.
- the water found above the filter 13 will flow downwards through the filter. If the raw water contains, say, iron or manganese, this will be oxidised by the admixed air, and the resulting oxides are all but insoluble in water. The resulting precipitate is inter ⁇ cepted by the sand filter 13, and the magazine 15 will thus contain clean, clear water.
- the relay 8 activates the first pump 7, so that raw water is again supplied to the tank 1 by the ejector 3.
- the filter 13 has to be backwashed at regular inter ⁇ vals. This is brought about by having the timer of the control system 24 cause the motor 19 of the second pump 18 to be deactivated at intervals, while at the same time the solenoid valve 23 is opened. Owing to the presetting of the timer of the control system, backwashing of the filter can be performed at any water level whatsoever in the tank. If the water level is low, there is a risk that the pressure in the pressure tank will not be sufficient to raise the level up to the overflow 31, such that the siphon begins to operate and the oily film can flow out.
- the control system is there ⁇ fore so designed that the pump 7 is always activated if the water level is located between the electrodes 9 and 10.
- the replenishment with raw water contributes to rapidly raising the water level to such an extent that the siphon and the overflow may begin to operate. It should be observed that the pump 7 is deactivated when the water level reaches the electrode 9.
- the water level in the tank sinks because the siphon continues to operate until the water reaches the opening of the siphon, which then begins to draw air.
- the end of the electrode 10 is locat ⁇ ed immediately below the siphon, and the electrode 10 activates the pump 7 when the water level sinks below this end.
Landscapes
- Chemical & Material Sciences (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)
- Organic Chemistry (AREA)
- Hydroponics (AREA)
- Filtration Of Liquid (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
Description
Claims
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU15947/95A AU1594795A (en) | 1994-01-25 | 1995-01-25 | Plant that purifies water from iron and manganese by aeration and filtration |
| SE9602515A SE507937C2 (en) | 1994-01-25 | 1996-06-26 | Water purificn. plant for removing iron and manganese |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SE9400206A SE9400206D0 (en) | 1994-01-25 | 1994-01-25 | Procedure for purification of water and water purification plant for carrying out the process |
| SE9400206-0 | 1994-01-25 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1995019937A1 true WO1995019937A1 (en) | 1995-07-27 |
Family
ID=20392668
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/SE1995/000071 Ceased WO1995019937A1 (en) | 1994-01-25 | 1995-01-25 | Plant that purifies water from iron and manganese by aeration and filtration |
Country Status (3)
| Country | Link |
|---|---|
| AU (1) | AU1594795A (en) |
| SE (1) | SE9400206D0 (en) |
| WO (1) | WO1995019937A1 (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2128146C1 (en) * | 1997-06-18 | 1999-03-27 | Ваид Амирджанович Керимов | Plant for purification of water from ferrum and manganese |
| RU2147014C1 (en) * | 1998-12-07 | 2000-03-27 | Научно-исследовательский технологический институт углеродных сорбентов | Drinking water purification process |
| EP1188721A1 (en) * | 2000-09-08 | 2002-03-20 | Uwe Dipl.-Ing. Würdig | Process and device for water treatment |
| RU2329955C2 (en) * | 2006-06-26 | 2008-07-27 | Открытое акционерное общество "Межотраслевой научно-исследовательский и проектно-технологический институт экологии топливно-энергетического комплекса" (ОАО "МНИИЭКО ТЭК") | Method of purification of sewage and natural water from ions of sulfate bivalent iron |
| RU2330815C2 (en) * | 2006-06-26 | 2008-08-10 | Открытое акционерное общество "Межотраслевой научно-исследовательский и проектно-технологический институт экологии топливно-энергетического комплекса" (ОАО "МНИИЭКО ТЭК") | Method of purification of sewage and natural waters from sulfate ions of divalent iron |
| CN101974933A (en) * | 2010-07-28 | 2011-02-16 | 苏州顶裕节能设备有限公司 | Overflow siphon automatic blow-down device |
| CN104787822A (en) * | 2015-05-06 | 2015-07-22 | 湖州天濮环保科技有限公司 | Sewage separating device |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SE160169C1 (en) * | ||||
| DE254857C (en) * | ||||
| US2237711A (en) * | 1938-05-12 | 1941-04-08 | Crane Company Of Minnesota | Purification of water |
| FI78143B (en) * | 1987-12-10 | 1989-02-28 | Matti Karhumaeki | Treatment process for household water in pressurized water systems in small buildings and a device for the application of the process |
-
1994
- 1994-01-25 SE SE9400206A patent/SE9400206D0/en unknown
-
1995
- 1995-01-25 WO PCT/SE1995/000071 patent/WO1995019937A1/en not_active Ceased
- 1995-01-25 AU AU15947/95A patent/AU1594795A/en not_active Abandoned
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SE160169C1 (en) * | ||||
| DE254857C (en) * | ||||
| US2237711A (en) * | 1938-05-12 | 1941-04-08 | Crane Company Of Minnesota | Purification of water |
| FI78143B (en) * | 1987-12-10 | 1989-02-28 | Matti Karhumaeki | Treatment process for household water in pressurized water systems in small buildings and a device for the application of the process |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2128146C1 (en) * | 1997-06-18 | 1999-03-27 | Ваид Амирджанович Керимов | Plant for purification of water from ferrum and manganese |
| RU2147014C1 (en) * | 1998-12-07 | 2000-03-27 | Научно-исследовательский технологический институт углеродных сорбентов | Drinking water purification process |
| EP1188721A1 (en) * | 2000-09-08 | 2002-03-20 | Uwe Dipl.-Ing. Würdig | Process and device for water treatment |
| RU2329955C2 (en) * | 2006-06-26 | 2008-07-27 | Открытое акционерное общество "Межотраслевой научно-исследовательский и проектно-технологический институт экологии топливно-энергетического комплекса" (ОАО "МНИИЭКО ТЭК") | Method of purification of sewage and natural water from ions of sulfate bivalent iron |
| RU2330815C2 (en) * | 2006-06-26 | 2008-08-10 | Открытое акционерное общество "Межотраслевой научно-исследовательский и проектно-технологический институт экологии топливно-энергетического комплекса" (ОАО "МНИИЭКО ТЭК") | Method of purification of sewage and natural waters from sulfate ions of divalent iron |
| CN101974933A (en) * | 2010-07-28 | 2011-02-16 | 苏州顶裕节能设备有限公司 | Overflow siphon automatic blow-down device |
| CN104787822A (en) * | 2015-05-06 | 2015-07-22 | 湖州天濮环保科技有限公司 | Sewage separating device |
| CN104787822B (en) * | 2015-05-06 | 2016-12-07 | 浙江天濮环保科技有限公司 | A kind of sewage separating device |
Also Published As
| Publication number | Publication date |
|---|---|
| AU1594795A (en) | 1995-08-08 |
| SE9400206D0 (en) | 1994-01-25 |
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