CN2934220Y - Well pump pneumatic direct-supplying deironing demanganizing equipment - Google Patents
Well pump pneumatic direct-supplying deironing demanganizing equipment Download PDFInfo
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- CN2934220Y CN2934220Y CN 200620021096 CN200620021096U CN2934220Y CN 2934220 Y CN2934220 Y CN 2934220Y CN 200620021096 CN200620021096 CN 200620021096 CN 200620021096 U CN200620021096 U CN 200620021096U CN 2934220 Y CN2934220 Y CN 2934220Y
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- water
- pipeline
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- well pump
- tank
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- Treatment Of Water By Oxidation Or Reduction (AREA)
- Removal Of Specific Substances (AREA)
Abstract
The utility model relates to a deferrization and demanganization device with direct supply of air pressure by well pump. Presently, the unergruond water deferrization and demanganization device comprises a deep well pump, an aeration tower, an aeration tank, a secondary booster pump, a filter, a clean water tank, a reaction water pump, an electric control system and a pipeline with complex process, complicated structure, repeated power consumption and easy pollution to water quality. Moreover, the unergruond water deferrization and demanganization device can only supply water with water supply equipment. The utility model comprises a deep well pump 1, a close and open type water supply tank 2, an aeration device 3, a reaction water pump 6, a filtering tank 5 and a distribution cabinet 8. The deep well pump 1 is connected to water intake of the water supply tank 2 via pipeline 10 arranged with the aeration device 3 and the check valve 4. The outlet of the close and open type water supply tank 2 is connected to the water intake of the filtering tank 5 via the pipeline 11 connected with the check valve 19. Moreover, the close and open type water supply tank 2 is connected to the outlet of the filtering tank 5 via the pipeline 12 connected with the reaction water pump 6 and the gate valve 7. The product is applied for underground deferrization and demanganization.
Description
Technical field:
The utility model relates to a kind of well pump air pressure direct supply type equipment of removing iron and manganese, is after utility model ZL200520021410.0 " well pump frequency conversion direct supply type equipment of removing iron and manganese ", another green energy conservation product.
Background technology:
Underground water deferrization and demanganization, it is one of vital task of building a New Socialist Countryside, the ultimate principle of its water treatment is: the catalysis crown_interception of the low price iron in the underground water, mn ion process ingress of air and filtrate, the high price iron, the manganic compound that are oxidized to could be held back by filter material layer, therefore, aeration and filtration are the gordian techniquies of deferrization and demanganization.At present, existing underground water deferrization and demanganization equipment is to be made of drowned pump, aeration tower, aeration tank, secondary pressing pump, strainer, filtered water tank, backwash pump, electrical control system and pipeline fitting, cause that middle-chain is many, structure is huge, repeat power consumption, unavoidable water quality recontaminate.The more important thing is that they do not possess the ability that supplies water to the user, also need dispose feedwater equipment.
Summary of the invention:
The purpose of this utility model provides a water lift deferrization and demanganization of a kind of energy direct-furnish user's well pump air pressure direct supply type equipment of removing iron and manganese.
Above-mentioned purpose realizes by following technical scheme:
Well pump air pressure direct supply type equipment of removing iron and manganese, its composition comprises: drowned pump, make and break formula are given water pot, aerating apparatus, backwash pump, filter tank and power distribution cabinet, described drowned pump is connected for the water pot water-in by pipeline and make and break formula, aerating apparatus and reverse checkvalve 4 are housed on the described pipeline, described make and break formula is connected for the water pot water outlet with the filter tank water-in by pipeline, be connected to reverse checkvalve on the described pipeline, described make and break formula also is connected for the water pot water outlet with the filter tank water outlet by pipeline, be connected to backwash pump and gate valve on the described pipeline.
Above-mentioned well pump air pressure direct supply type equipment of removing iron and manganese, described filter tank top is connected to the sewage backwash pipeline, and described make and break formula feedwater pot sidewall is equipped with electro connecting pressure gauge.
Above-mentioned well pump air pressure direct supply type equipment of removing iron and manganese, described power distribution cabinet one end is connected with power supply with lead, and the other end is connected with described drowned pump, described electro connecting pressure gauge, described aerating apparatus respectively with lead.
Above-mentioned well pump air pressure direct supply type equipment of removing iron and manganese is equipped with filtrate and water in the described filter tank.
This technical scheme has following beneficial effect:
1. deferrization and demanganization process flow process of the present utility model is:
The pipeline aeration
↓
Drowned pump → make and break formula is given water pot → filter tank → user
↓ ↑
-backwash pump-
Obviously, the utility model can a water lift deferrization and demanganization direct-furnish user.
2. the utility model is simple in structure, and is easy to control, and casualty ratio of accidents is low, and economize on electricity 30-50% saves total investment for construction 30-50%.
3. in conjunction with working process structural advantages of the present utility model is described:
Normal service condition:
The pointer of electro connecting pressure gauge 9 is between lower limit start-up point and upper limit arrests, user's water, enclosed enters user's pipe network by filter tank 5 for the dissolved oxygen water in the water pot 2 under the elastic force of control air, the make and break formula reduces for water pot 2 internal pressures, when the pointer of electro connecting pressure gauge 9 is run into down in limited time, drowned pump 1 starts, aerating apparatus 3 work, in pipeline 10, inject excessive air, participate in the oxidation of iron and manganese on the one hand, control air is provided for water pot 2 to the make and break formula on the other hand, give in the water pot 2 along with the air water mixed solution enters the make and break formula, electro connecting pressure gauge 9 pointers rise, when running into upper limit arrests, drowned pump 1 stops, this process is back and forth moved, can be constantly to user's automatic water-supply, and in this process, the catalysis of phreatic aeration process and filtrate is held back process and is all carried out at the same time, reaches the purpose of well pump air pressure direct supply type deferrization and demanganization thus.
The back flushing state:
The artificial filtrate of setting in the filter tank 5 is held back foul to and is finalized a text when measuring, be decided to be a backwashing period, slowly open gate valve 18, discharging make and break formula is given the about 2/3 volume gas in the water pot 2, fills with water for water pot 2 the make and break formula thereupon, open gate valve 7 and gate valve 15, manually boot the filtrate in the backwash pump 6 flushing filter tanks 5, exhaust for water pot 2 interior water to the make and break formula and stop, this process 1-3 jar water finishes, recover normal service condition, make this product to recycle.
4. the utility model effect: application in practice: be provided with place's deep well, its underground water content 10 mg/litre, exceed 30 times than national drinking water standard Fe≤0.3 mg/litre, manganese content 1.5 mg/litre, exceed 15 times than national drinking water standard Mn≤0.1 mg/litre, 10 tons/hour of the flows of drowned pump, the residue lift is 40 meters, can satisfy this area's domestic water for residents.Now select one of filter tank, the volume 4m of diameter phi 1400mm
3The make and break formula forms well pump air pressure direct supply type equipment of removing iron and manganese for one of water pot, one of ISG800-100 (I) backwashing pump, SLB-20 aerating apparatus one cover, and its operating parameter is:
(1). aeration rate is abundant.
(2). the MnO in the manganese sand filtering material
2〉=35%, maximum rate of filtering is less than 8 meters/hour.
(3). back washing strength 16-18 liter/second square metre.
(4). the drowned pump per hour number of starts is less than 6 times.
Theory and practice proves that well pump air pressure direct supply type equipment of removing iron and manganese is feasible, compares with conventional art to have significant technical progress.
Description of drawings:
Accompanying drawing 1 is the structural representation of this product.
Embodiment:
Embodiment 1:
Well pump air pressure direct supply type equipment of removing iron and manganese, its composition comprises: drowned pump 1, the make and break formula is given water pot 2, aerating apparatus 3, backwash pump 6, filter tank 5 and power distribution cabinet 8, described drowned pump 1 is connected for water pot 2 water-ins by pipeline 10 and make and break formula, aerating apparatus 3 and reverse checkvalve 4 are housed on the described pipeline 10, described make and break formula is connected for water pot 2 water outlets with filter tank 5 water-ins by pipeline 11, be connected to reverse checkvalve 19 on the described pipeline 11, described make and break formula also is connected for water pot 2 water outlets with filter tank 5 water outlets by pipeline 12, be connected to backwash pump 6 and gate valve 7 on the described pipeline 12.
Embodiment 2:
Above-mentioned well pump air pressure direct supply type equipment of removing iron and manganese, described filter tank 5 tops are connected to sewage backwash pipeline 13, and described sewage backwash pipeline 13 is connected with blow-off line through gate valve 15, and described make and break formula is equipped with electro connecting pressure gauge 9 for water pot 2 sidewalls.
Embodiment 3:
Above-mentioned well pump air pressure direct supply type equipment of removing iron and manganese, described power distribution cabinet 8 one ends are connected with power supply with lead, and the other end is connected with described drowned pump 1, described electro connecting pressure gauge 9, described aerating apparatus 3 respectively with lead.
Embodiment 4:
Above-mentioned well pump air pressure direct supply type equipment of removing iron and manganese is equipped with filtrate and water in the described filter tank 6, and described filter tank 5 rising pipes 14 are connected with user's pipe network by gate valve 16.
Embodiment 5:
Above-mentioned well pump air pressure direct supply type equipment of removing iron and manganese, described make and break formula is provided with the breathing pipeline 17 that leads to the outside for the topmost of water pot 2, and described pipeline 17 ports are provided with gate valve 18, when gate valve 18 is closed, be the enclosed water supply tank of atmospheric pressure, be used in the normal water supply state; When gate valve 18 is opened, for the open type normal pressure is given water pot, as manganese sand back flushing Water-storage tank, one jar of dual-purpose.
Claims (4)
1. well pump air pressure direct supply type equipment of removing iron and manganese, its composition comprises: drowned pump, the make and break formula is given water pot, aerating apparatus, backwash pump, filter tank and power distribution cabinet, it is characterized in that: described drowned pump is connected for the water pot water-in by pipeline and make and break formula, aerating apparatus and reverse checkvalve are housed on the described pipeline, described make and break formula is connected for the water pot water outlet with the filter tank water-in by pipeline, be connected to reverse checkvalve on the described pipeline, described make and break formula also is connected for the water pot water outlet with the filter tank water outlet by pipeline, be connected to backwash pump and gate valve on the described pipeline.
2. well pump air pressure direct supply type equipment of removing iron and manganese according to claim 1, it is characterized in that: described filter tank top is connected to the sewage backwash pipeline, and described make and break formula feedwater pot sidewall is equipped with electro connecting pressure gauge.
3. well pump air pressure direct supply type equipment of removing iron and manganese according to claim 1 and 2, it is characterized in that: described power distribution cabinet one end is connected with power supply with lead, and the other end is connected with described drowned pump, described electro connecting pressure gauge, described aerating apparatus respectively with lead.
4. well pump air pressure direct supply type equipment of removing iron and manganese according to claim 2 is characterized in that: filtrate and water are housed in the described filter tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200620021096 CN2934220Y (en) | 2006-06-26 | 2006-06-26 | Well pump pneumatic direct-supplying deironing demanganizing equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200620021096 CN2934220Y (en) | 2006-06-26 | 2006-06-26 | Well pump pneumatic direct-supplying deironing demanganizing equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2934220Y true CN2934220Y (en) | 2007-08-15 |
Family
ID=38350908
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200620021096 Expired - Fee Related CN2934220Y (en) | 2006-06-26 | 2006-06-26 | Well pump pneumatic direct-supplying deironing demanganizing equipment |
Country Status (1)
Country | Link |
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CN (1) | CN2934220Y (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103850288A (en) * | 2014-04-02 | 2014-06-11 | 哈尔滨市旭东给水技术有限责任公司 | Sanitary water transmission and distribution apparatus capable of removing iron and manganese |
CN105887973A (en) * | 2016-06-15 | 2016-08-24 | 栾海沫 | Iron and manganese removal type energy saving water conveying and distribution equipment and water supply method |
-
2006
- 2006-06-26 CN CN 200620021096 patent/CN2934220Y/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103850288A (en) * | 2014-04-02 | 2014-06-11 | 哈尔滨市旭东给水技术有限责任公司 | Sanitary water transmission and distribution apparatus capable of removing iron and manganese |
CN103850288B (en) * | 2014-04-02 | 2016-01-13 | 哈尔滨市旭东给水技术有限责任公司 | Deferrization and demanganization formula health transmission & distribution wetting system |
CN105887973A (en) * | 2016-06-15 | 2016-08-24 | 栾海沫 | Iron and manganese removal type energy saving water conveying and distribution equipment and water supply method |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070815 Termination date: 20150626 |
|
EXPY | Termination of patent right or utility model |