CN2928830Y - Pressure magnetizing micro porous filter material filtering iron removing and manganesium removing device - Google Patents
Pressure magnetizing micro porous filter material filtering iron removing and manganesium removing device Download PDFInfo
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- CN2928830Y CN2928830Y CN 200520093731 CN200520093731U CN2928830Y CN 2928830 Y CN2928830 Y CN 2928830Y CN 200520093731 CN200520093731 CN 200520093731 CN 200520093731 U CN200520093731 U CN 200520093731U CN 2928830 Y CN2928830 Y CN 2928830Y
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- water
- valve
- pump
- strainer
- iron
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- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
A pressure-type magnetic micro-pore filtering material filtration device for iron and manganese removal is characterized in that an aerator is connected with the inlet of a water tank whose outlet is connected with the inlet of a strong magnetizer via an operation pump and a backwash pump, which are joined in parallel. The outlet of the strong magnetizer is divided into 1-n ways, which are respectively connected with inlets of 1-n filters whose outlets are connected with a general exhaust pipe, wherein the general exhaust pipe is simultaneously connected with a general exhaust valve and a forthwash blow-down valve respectively. The backwash pump is connected with the outlet of the filter via a backwash valve and the inlet of the filter is connected with a backwash blow-off valve simultaneously. The filter, provided with an outlet at the bottom, an air-vent and an inlet on the top, is filled with micro-pore filtering material. The utility model has the advantages of rapid iron removal and good effect.
Description
Technical field:
The utility model relates to water technology, and a kind of pressure type magnetization micropore media filtration facility for iron and manganese removal from is provided especially.
Background technology:
Iron is the necessary trace element of human body, in case the human body iron deficiency can get diseases such as hypoferric anemia, directly influences healthy.Needed iron is mainly derived from food and drinking-water in the human body, contains a certain amount of iron in the water and the people is had a mind to harmless.Yet iron-holder is too much in the water, also can work the mischief.Measure according to relevant department, when there not being any peculiar smell in the water during iron-holder 0.3mg/l; During iron-holder 0.5mg/l, colourity can reach more than 30 degree; During iron-holder 1.0m/l, not only colourity increases, and has tangible Metallic Flavour.When the concentration of iron surpasses certain limit, will produce throw out russet, can stay macula lutea on white fabrics or water vessel, sanitary apparatus in the life, also make the iron bacteria breeding simultaneously easily, blocking pipe reduces conveyance power of water; Industrial, when being used for industries such as weaving, printing and dyeing, knitting, papermaking, can influence quality product.Particularly the tap water iron-holder is too much, can cause stomach malaise symptoms such as poor appetite, vomiting, diarrhoea.According to another the current research result, iron is too much harmful to heart in the human body.Therefore the excessive iron of removing in the high molten iron is very important.
Summary of the invention:
The purpose of this utility model is to provide a kind of pressure type magnetization micropore media filtration facility for iron and manganese removal from, and its deironing is rapid, and is effective.
The utility model provides a kind of pressure type magnetization micropore media filtration facility for iron and manganese removal from, mainly by aerator (1), water tank (2), process pump (3), backwashing pump (4), a force-magnetized device (5), 1~n strainer constitutes, it is characterized in that: aerator (1) joins with the water inlet of water tank (2), the water outlet warp of water tank (3) and the operation water pump (3) that connects link to each other with force-magnetized device (5) water inlet with backwashing pump (4) again, force-magnetized device (5) water outlet is divided into 1~n road and links to each other with 1~n strainer water inlet respectively, the water outlet of 1~n strainer is connected on total rising pipe, total rising pipe is simultaneously respectively with total flowing water Valve F13 with just washing sewage draining valve F14 and join, backwashing pump (4) is simultaneously by valve F9, F11, F12 links to each other with the water outlet of strainer, and the strainer water inlet links to each other with backwash sewage draining valve F10 simultaneously; Fill the micropore filtrate in the described strainer, the bottom sets out the mouth of a river, and the top is provided with venting port, and water inlet is arranged at the epimere of strainer.
In the utility model pressure type magnetization micropore media filtration facility for iron and manganese removal from, at the preceding penstock F1 that taps into of described aerator (1); Behind described operation water pump (3), meet operation water pump reverse stop valve F4, operation water pump water outlet valve F5; Behind described backwashing pump (4), meet backwashing pump reverse stop valve F6, backwashing pump flowing water Valve F7.
In the utility model pressure type magnetization micropore media filtration facility for iron and manganese removal from, water distribution board (8), following water distribution board (9) are set, the middle filtrate (10) of placing in the strainer (6).
Force-magnetized device (5) adopts Chinese patent ZL97231378.8 structure in the utility model.
High molten iron generally is present in the deep phreatic water, because underground water anoxic, basicity are higher, so the iron in the underground water is mainly with the ferrous Fe (HCO of unsettled heavy carbonic
3)
2Exist.Ferrous iron does not develop the color, so just very clear from the underground water that comes that draws up.When iron content underground water touches air, airborne oxygen rapidly and the ferrous iron in the water combine, be oxidized to the ferric iron that is insoluble in water and from water, separate out, Here it is high molten iron that we saw as tea.
The utility model make high molten iron through aerator (1) again through force-magnetized device (5), make dissolved oxygen amount, the dioxygen water yield and pH value in the high molten iron that raising all be arranged, thereby accelerated ferrous oxidation rate in the high molten iron, the water polymerization degree after magnetization is significantly improved in addition, can accelerate the clarifying speed of iron ion greatly, help the removal of iron.Therefore the utlity model has deironing speed faster and de-ferrous effect preferably.Below by embodiment in detail the utility model is described in detail.
Description of drawings:
Accompanying drawing 1 is pressure type magnetization micropore media filtration facility for iron and manganese removal from structural representation.
Embodiment:
Embodiment
As shown in Figure 1, pressure type magnetization micropore media filtration facility for iron and manganese removal from mainly is made of aerator (1), water tank (2), strainer A (6), filter B (7), a force-magnetized device (5); The preceding penstock F1 that taps into of aerator (1), aerator (1) joins with the water inlet of water tank (2), the water outlet of water tank (2) through and the operation water pump (3) that connects and backwashing pump (4) again with force-magnetized device (5), water inlet valve F8 links to each other with force-magnetized device (5) water inlet, force-magnetized device (5) water outlet be divided into two-way respectively with strainer A (6), the water inlet of filter B (7) links to each other, strainer A (6), the water outlet of filter B (7) passes through the flowing water Valve F11 of two strainers respectively, F12 is connected on total rising pipe, respectively with total flowing water Valve F13 with just washing sewage draining valve F14 and join, backwashing pump (4) links to each other with total rising pipe by backwash valve F9 total rising pipe simultaneously simultaneously; Fill micropore filtrate (10) in the hay tank (6), the bottom sets out the mouth of a river, and the top sets into the mouth of a river, and the venting port and the drain tap F15 of hay tank (6) join.Meet operation water pump water outlet valve F5, operation water pump reverse stop valve F4 behind the operation water pump (3), connect backwash water behind the backwashing pump (8) and pump penstock F7, backwash water pump check valve door F6.Specified operational procedure is as follows:
1, flushing filtrate
Before device first puts into operation, at first to wash, the dust dirt in the filtrate is rinsed well, till flowing out clear water filtrate.During flushing, start the backwash water pump two strainers are washed separately.
When with backwashing pump (4) washing and filtering device A (6), want valve-off F5, F8, F12, F13, F14 earlier, open valve F7, F9, F11, F10, start backwash water pump (4) then.Please note when flowing out filtrate in the blow-off pipe of valve F10, should adjust valve F9, reduce flushing flow rate.
When with backwashing pump (4) washing and filtering device B (7), do not need termination of pumping, on the basis of washing and filtering device A (6), open valve F12, valve-off F11 gets final product.
When equipment normally moved, the step of back flushing was same as described above.
2, just wash before the operation
Start operation water pump (3), when washing filtrate, because the iron in the former water also without purifying treatment, before putting into operation, should be got rid of the former water in the strainer by sewage draining valve F14 with former water.When water became clear, the water after will purifying was again delivered to pipe network or water tower.
When just washing before the operation, two strainers are worked simultaneously.Under the state of washing and filtering device B (7), valve F5, F8, F11, F14 are opened in first termination of pumping, valve-off F7, F9, F10.
3, normal operation
When sewer becomes clear after just washing, can formally put into operation, send water to the user.Just washing under the state not termination of pumping, Open valve F13, valve-off F14.
More than each schedule of operation must strict carry out, otherwise may cause the damage of water pump, motor.
Claims (3)
1, a kind of pressure type magnetization micropore media filtration facility for iron and manganese removal from, mainly by aerator (1), water tank (2), process pump (3), backwashing pump (4), a force-magnetized device (5), 1~n strainer constitutes, it is characterized in that: aerator (1) joins with the water inlet of water tank (2), the water outlet warp of water tank (3) and the operation water pump (3) that connects link to each other with force-magnetized device (5) water inlet with backwashing pump (4) again, force-magnetized device (5) water outlet is divided into 1~n road and links to each other with 1~n strainer water inlet respectively, the water outlet of 1~n strainer is connected on total rising pipe, total rising pipe is simultaneously respectively with total flowing water Valve F13 with just washing sewage draining valve F14 and join, backwashing pump (4) is simultaneously by valve F9, F11, F12 links to each other with the water outlet of strainer, and the strainer water inlet links to each other with backwash sewage draining valve F10 simultaneously; Fill the micropore filtrate in the described strainer, the bottom sets out the mouth of a river, and the top is provided with venting port, and water inlet is arranged at the epimere of strainer.
2, according to the described pressure type magnetization of claim 1 micropore media filtration facility for iron and manganese removal from, it is characterized in that: at the preceding penstock F1 that taps into of described aerator (1); Behind described operation water pump (3), meet operation water pump reverse stop valve F4, operation water pump water outlet valve F5; Behind described backwashing pump (4), meet backwashing pump reverse stop valve F6, backwashing pump flowing water Valve F7.
3, according to the described pressure type magnetization of claim 1 micropore media filtration facility for iron and manganese removal from, it is characterized in that: water distribution board (8), following water distribution board (9) are set, the middle filtrate (10) of placing in the strainer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200520093731 CN2928830Y (en) | 2005-11-22 | 2005-11-22 | Pressure magnetizing micro porous filter material filtering iron removing and manganesium removing device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN 200520093731 CN2928830Y (en) | 2005-11-22 | 2005-11-22 | Pressure magnetizing micro porous filter material filtering iron removing and manganesium removing device |
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CN2928830Y true CN2928830Y (en) | 2007-08-01 |
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CN 200520093731 Expired - Fee Related CN2928830Y (en) | 2005-11-22 | 2005-11-22 | Pressure magnetizing micro porous filter material filtering iron removing and manganesium removing device |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102020390B (en) * | 2009-09-10 | 2012-09-19 | 李明 | Magnetoelectric nanofiltration sewage purification system and purification process |
CN104724875A (en) * | 2013-12-24 | 2015-06-24 | 沈阳市天泉水处理设备有限责任公司 | Pressure type magnetization SS filtering material filtration iron removal and manganese removal device |
-
2005
- 2005-11-22 CN CN 200520093731 patent/CN2928830Y/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102020390B (en) * | 2009-09-10 | 2012-09-19 | 李明 | Magnetoelectric nanofiltration sewage purification system and purification process |
CN104724875A (en) * | 2013-12-24 | 2015-06-24 | 沈阳市天泉水处理设备有限责任公司 | Pressure type magnetization SS filtering material filtration iron removal and manganese removal device |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |