CN106365295B - Facility for iron and manganese removal and microbe filter method based on microorganism - Google Patents
Facility for iron and manganese removal and microbe filter method based on microorganism Download PDFInfo
- Publication number
- CN106365295B CN106365295B CN201610771556.XA CN201610771556A CN106365295B CN 106365295 B CN106365295 B CN 106365295B CN 201610771556 A CN201610771556 A CN 201610771556A CN 106365295 B CN106365295 B CN 106365295B
- Authority
- CN
- China
- Prior art keywords
- water
- iron
- filter
- manganese
- aeration
- 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.)
- Active
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/06—Aerobic processes using submerged filters
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F2003/001—Biological treatment of water, waste water, or sewage using granular carriers or supports for the microorganisms
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
- C02F2101/203—Iron or iron compound
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
- C02F2101/206—Manganese or manganese compounds
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Biodiversity & Conservation Biology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
The invention discloses a kind of facility for iron and manganese removal based on microorganism and microbe filter method, which includes the first immersible pump, aeration tank, microbial deactivation apparatus, the second immersible pump, recoil wash pool, clear water reserviors, water tank and aerator;The first immersible pump is provided between the aeration tank and missile silo, aeration tank is equipped with aerator, and aerator includes the air pressure pump and aeration plate connected by aerated conduit, and the upper end of aeration plate is provided with pulling apparatus;The aeration tank and microbial deactivation apparatus are linked in sequence, and the lower end of microbial deactivation apparatus is provided with outlet threeway and connect respectively with recoil wash pool and clear water reserviors, are provided with the second immersible pump between the wash pool that recoils and outlet threeway;The microbial deactivation apparatus includes top cover, filter column, bottom cover and cross traveling trolley, and top cover, filter column and bottom cover connect from top to bottom, and to be detachably connected, cross traveling trolley is used to support filter column;The water tank is connect with the overflow pipe on filter column top.
Description
Technical field
The present invention relates to a kind of water treatment field, more particularly to a kind of facility for iron and manganese removal based on microorganism and micro-
Biologic filtration method.
Background technique
China has in the underground water in many areas, and the content of iron and manganese is higher, is more than or considerably beyond Drinking Water
Sanitary standard and standards for industrial water usage, to seriously affect its use value, it is therefore necessary to be removed.
Currently, the water treatment of underground water mostly uses greatly microorganism deferrization and demanganization, but in microorganism deferrization and demanganization process
In, the ferrous iron in underground water is oxidized to ferric oxide by chemical oxidation or iron-oxidizing bacteria, is attached on filtrate or is filtered
Material is intercepted;Bivalent manganese is oxidized to manganese dioxide by manganese oxidizing bacteria, is attached on filtrate;And backwash can be by most iron oxygen
Compound and Mn oxide are rinsed out from filtrate, guarantee the normal filtration effect of filter column.But existing microorganism deferrization and demanganization dress
The filter device set is an integral structure mostly, it has not been convenient to be checked the service condition of intermediate filter column, and be replaced intermediate filter column;Its
It is secondary, some manganese oxidizing bacterias and iron-oxidizing bacteria are contained in backwashing water, can be externally discharged with backwashing water, lead to the wave of resource
Take;In addition, existing aerator is all inaccurate to the concentration control of dissolved oxygen in underground water, lead to energy waste.
Summary of the invention
For the defects in the prior art, the present invention provides a kind of facility for iron and manganese removal based on microorganism and microorganism mistake
Filtering method can be recycled and contain manganese oxidizing bacteria and iron-oxidizing bacteria in backwashing water, the accurate dissolved oxygen for controlling underground water in aeration tank
Concentration.
A kind of underground water deferrization and demanganization device, including the first immersible pump, aeration tank, microbial deactivation apparatus, the second diving
Pump, recoil wash pool, clear water reserviors, water tank and aerator;It is provided with the first immersible pump between the aeration tank and missile silo, exposes
Equipped with aerator, aerator includes the air pressure pump and aeration plate connected by aerated conduit, aerated conduit in gas pond
On be provided with flowmeter, aeration plate is located at the top of aeration tank, and the upper end of aeration plate is provided with pulling apparatus, and on aeration plate
It is even to be disposed with equidistant exhaust pipe, equidistant gas vent has been evenly arranged on exhaust pipe;The aeration tank and microorganism
Filter device is linked in sequence, and the lower end of microbial deactivation apparatus is provided with outlet threeway and connects respectively with recoil wash pool and clear water reserviors
It connects, is provided with the second immersible pump between the wash pool that recoils and outlet threeway;The microbial deactivation apparatus includes top cover, filter column, bottom
Lid and cross traveling trolley, top cover, filter column and bottom cover connect from top to bottom, and to be detachably connected, cross traveling trolley is used to support filter column;Institute
Water tank is stated to connect with the overflow pipe on filter column top;The top cover upper end is provided with water inlet pipe, in water inlet pipe and top cover
The spray equipment in portion is connected;The filter column includes column shell, filtrate and bottom plate, and the top of the column shell is provided with overflow pipe,
The ears or side handles of a utensil are provided in the middle part of column shell, bottom plate is in cellular, is arranged in the lower end of column shell, and the aperture on bottom plate is 0.3-0.5mm;Institute
Stating filtrate is microorganism carrier, and filtrate includes bed course and filter layer, and filter layer, bed course and bottom plate are in upper and lower cloth in filter housing
It sets;The lower end of the bottom cover is provided with outlet threeway and foot prop;The cross traveling trolley includes framework platform and support frame, and frame is flat
Platform is rectangle frame structure, on framework platform setting there are two the storage position for placing filter column, be provided in storage position with
The locating slot of ears or side handles of a utensil adaptation in the middle part of column shell, the four corners of framework platform and four support frames vertically connect, four support frames
It is respectively arranged with lifting or declines the electric cylinder of framework platform, the foot of support frame is provided with castor.
Preferably, the aeration tank uses weak gas explosion, and the concentration of the dissolved oxygen after aeration in water is 4-6mg/L.
Preferably, the top cover top is provided with air vent and drain hole, and air vent upper end is provided with movable port lid.
Preferably, it is respectively arranged between the outlet threeway and the second immersible pump and clear water reserviors of the microbial deactivation apparatus
Backwash ball valve and clear water reserviors ball valve.
Preferably, the filter layer of the filtrate has been sequentially arranged quartz sand, manganese sand and active carbon particle from bottom to up, quartz
The partial size of sand, manganese sand and active carbon particle is 0.6-1.5mm, and the mass ratio of quartz sand, manganese sand and active carbon particle is 5:3:2.
Preferably, it is provided with sealing ring between the top cover and bottom cover and filter column, entrance ball is provided on water inlet pipe
Valve.
Preferably, the column shell uses glass steel material, and top cover and bottom cover use stainless steel.
The present invention also provides a kind of filter methods using above-mentioned underground water deferrization and demanganization device, comprising the following steps:
Underground water is extracted in aeration tank by the first immersible pump, after the weak aeration in aeration tank, so that the dissolved oxygen in underground water
Reach 4-6mg/L;The underground water after weak aeration is transported to microbial deactivation apparatus again, filtering velocity 5-7m/h, in underground water
The iron-oxidizing bacteria and manganese oxidizing bacteria that ferrous iron and bivalent manganese can be attached on filtrate are oxidized into ferric iron and manganic, from
And it is intercepted by filtrate;Domestic water standard is had reached through the filtered underground water of microbial deactivation apparatus, partially
It is lauched and is passed through spare in recoil wash pool, remaining underground water is then passed through in clear water reserviors as domestic water or industrial water;When micro-
The filtration time of biofiltration device reaches 24-48 hours, needs to be passed through the water in the wash pool that recoils by the second immersible pump micro-
It is backwashed in biofiltration device, backwashing time is 3-5 minutes, and back washing strength is 7-11L/ (sm2), to rinse
Fall the ferriferous oxide and Mn oxide adhered on filtrate, and is flowed into water tank by overflow pipe.
Preferably, iron-oxidizing bacteria and manganese oxidizing bacteria, underground water in filter column are contained in the backwashing water that the water tank is collected
Water level it is excessively high when water tank flowed by overflow pipe, the ferrous iron and bivalent manganese that contain in underground water are the iron oxygen of water tank
Change bacterium and manganese oxidizing bacteria provides the environment of life and breeding;After 3-6 days, iron-oxidizing bacteria and manganese oxidizing bacteria can be in the waters surface of water tank
Form colloid substance;Periodically this mucilage binding substance is added in filter column by the drain hole of top cover upper end.
The beneficial effects of the present invention are embodied in:
1. the microorganism that the present invention refers to mainly includes iron-oxidizing bacteria and manganese oxidizing bacteria, they are aerobic bacterias, so ground
The concentration of lower oxygen in water will seriously affect the filter efficiency of microorganism in filter device;The aeration tank is filled equipped with aeration
It sets, the air pressure pump in aerator delivers the air to aeration plate through aerated conduit, passes through the gas vent on exhaust pipe
Discharge, so that the oxygen in air is dissolved in underground water;Pass through the air of control flowmeter adjustable air compression pump output
Flow, to realize the dissolved oxygen concentration in accurate control underground water;Pulling apparatus can make aeration plate rise in aeration tank or
Decline, can be improved the uniformity of dissolved oxygen concentration in underground water in aeration tank;Aeration tank uses weak gas explosion, molten in water after aeration
The concentration for solving oxygen is controlled in 4-6mg/L, be ensure that the filter efficiency of microorganism, is reduced aeration cost, avoid waste of energy;
The water tank is used to collect underground water when water level is excessively high in backwashing water and filter column, aoxidizes in backwashing water containing some iron
Bacterium and manganese oxidizing bacteria contain ferrous iron and bivalent manganese in underground water;Therefore, iron-oxidizing bacteria and manganese oxidizing bacteria be can provide in water tank
Life and breeding environment, after a period of time, colloid substance, as iron-oxidizing bacteria and manganese oxygen can be formed in the water surface of water tank
Change bacterium;This colloid substance is added in filter column by drain hole periodically, the filtering effect of microbial deactivation apparatus can be improved
Fruit.
2. the cross traveling trolley setting is there are two storage position, storage position is provided with the positioning being adapted to the ears or side handles of a utensil in the middle part of column shell
Slot, it is convenient that filter column is replaced for placing and supporting filter column, to clean to the wall dirt inside filter column, it ensure that filter
The filter space of column avoids the obstruction of some bypass lines.
3. the filtrate is disposed with quartz sand, manganese sand and active carbon particle from bottom to top, filtrate is primarily as microorganism
Carrier, manganese sand can adsorb some heavy metals in the function of possessing demanganization, active carbon particle.
4. column shell top is provided with overflow pipe, for filter column water level inside excessively high water or backwashing water to be discharged.
5. top cover top is provided with air vent, air vent upper end is furnished with movable port lid, outside filter air pressure inside is greater than
When boundary's atmospheric pressure, port lid will be washed open by the gas of filter interior, to discharge gas excessive in filter, to guarantee
Filter inner and outer air pressure is consistent;Conversely, port lid will be in closed state, to prevent some sundries from falling into filter.
Detailed description of the invention
It, below will be to specific in order to illustrate more clearly of the specific embodiment of the invention or technical solution in the prior art
Attached drawing needed in embodiment is briefly described.In all the appended drawings, similar element or part are generally by class
As appended drawing reference identify.In attached drawing, each element or part might not be drawn according to actual ratio.
Fig. 1 is the structural schematic diagram of the embodiment of the present invention;
Fig. 2 is the structural schematic diagram of cross traveling trolley in the embodiment of the present invention.
In attached drawing, the first immersible pump of 1-, the aeration tank 2-, 21- aerator, 211- aeration plate, 212- aerated conduit, 213-
Air pressure pump, 214- flowmeter, 215- pulling apparatus, 3- microbial deactivation apparatus, 31- top cover, 311- Inlet ball valve, 312-
Water inlet pipe, 313- air vent, 314- port lid, 315- spray equipment, 316- drain hole, 32- filter column, 321- column shell, 322- filter
Material, 3221- bed course, 3222- filter layer, 323- bottom plate, the 324- ears or side handles of a utensil, 325- overflow pipe, 326- spilling water ball valve, 33- bottom cover,
331- outlet threeway, 332-foot props, 34- cross traveling trolley, 341- castor, 342- electric cylinder, 343- support frame, 344- frame are flat
Platform, 345- storage position, 346- locating slot, 4- clear water reserviors, 41- clear water reserviors ball valve, 5- recoil wash pool, 51- backwash ball valve, 52-
Second immersible pump, 6- missile silo, 7- water tank
Specific embodiment
It is described in detail below in conjunction with embodiment of the attached drawing to technical solution of the present invention.Following embodiment is only used for
Clearly illustrate technical solution of the present invention, therefore be only used as example, and cannot be used as a limitation the protection model of limitation this patent
It encloses.In addition, term " first ", " second " etc. be used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance or
Person implicitly indicates the quantity of indicated technical characteristic.
Such as Fig. 1 and Fig. 2, present embodiment discloses a kind of underground water deferrization and demanganization devices, including the first immersible pump 1, aeration
Pond 2, microbial deactivation apparatus 3, clear water reserviors 4, recoil wash pool 5, water tank 7 and aerator 21, aeration tank 2 and missile silo 6 it
Between be provided with the first immersible pump 1, the first immersible pump 1 can extract underground water in aeration tank 2.Aeration tank 2 is filled equipped with aeration
21 are set, the air pressure pump 213 and aeration plate 211 in aerator 21 are connected by aerated conduit 212, on aerated conduit 212
It is provided with flowmeter 214, aeration plate 211 is located at the top of aeration tank 2, and the upper end of aeration plate 211 is provided with pulling apparatus 215,
And equidistant exhaust pipe has been evenly arranged on aeration plate 211, equidistant gas vent has been evenly arranged on exhaust pipe.Air
Compression pump 213 delivers the air to aeration plate 211 through aerated conduit 212, is discharged by the gas vent on exhaust pipe, thus handle
Oxygen in air is dissolved in underground water;The air mass flow exported by control 214 adjustable air compression pump 213 of flowmeter,
To realize the dissolved oxygen concentration in accurate control underground water;Pulling apparatus 215 can be such that aeration plate 211 rises in aeration tank 2
Or decline, the uniformity of dissolved oxygen concentration in underground water in aeration tank 2 can be improved;Aeration tank 2 uses weak gas explosion, after aeration in water
Dissolved oxygen concentration control in 4-6mg/L, ensure that the filter efficiency of microorganism, reduce aeration cost, avoid waste
The energy.
Aeration tank 2 and microbial deactivation apparatus 3 are linked in sequence, and the lower end of microbial deactivation apparatus 3 is provided with outlet threeway
331 connect with clear water reserviors 4 and recoil wash pool 5 respectively.It is provided with clear water reserviors ball valve 41 between clear water reserviors 4 and outlet threeway 331, instead
It is provided with the second immersible pump 52 between flushing tank 5 and outlet threeway 331, is arranged between the second immersible pump 52 and outlet threeway 331
There is backwash ball valve 51, the water in the wash pool 5 that recoils can be transported to microbe filter by exporting threeway 331 by the second immersible pump 52
In device 3, to rinse out the most of ferriferous oxide and Mn oxide that adhere on filtrate 322.
Microbial deactivation apparatus 3 include top cover 31, filter column 32 and bottom cover 33, top cover 31, filter column 32 and bottom cover 33 from up to
Under be successively bolted, and sealing ring 5 is provided between three;Top cover 31 and bottom cover 33 are hemispherical, and using stainless
Steel material.31 upper end of top cover is provided with water inlet pipe 312, and Inlet ball valve 311, water inlet pipe 312 are provided on water inlet pipe 312
It is connected with the spray equipment 315 inside top cover 31, spray equipment 315 is in disk form, and water can be made to be evenly distributed in filter column 32,
Avoiding in filter column 32 leads to poor filtration effect because local water is big.
Filter column 32 includes column shell 321, filtrate 322 and bottom plate 323, and filtrate 322 is microorganism carrier, and filtrate 322 includes
The thickness ratio of bed course 3221 and filter layer 3222, bed course 3221 and filter layer 3222 is 1:5.In the present invention, bed course 3221 is used
Partial size is the cobble of 3-8mm.Certainly, bed course 3221 can also use gravel.Filter layer 3222, bed course 3221 and bottom plate 323 exist
It is sequentially arranged from top to bottom in column shell 321, bottom plate 323 is arranged in the lower end of column shell 321, the aperture on bottom plate 323 in cellular
For 0.3-0.5mm.Filter layer 3222 has been sequentially arranged quartz sand, manganese sand and active carbon particle from bottom to up, quartz sand, manganese sand and
The mass ratio of active carbon particle is 5:3:2, and the partial size of three is 0.6-1.5mm, and quartz sand reduces the cost of filtrate 322, manganese
Sand possesses the function of demanganization, and active carbon particle can adsorb some heavy metals, and quartz sand, manganese sand and active carbon particle are used as micro-
The carrier of biology.The lower end of bottom cover 33 is provided with outlet threeway 331 and foot prop 332.
Cross traveling trolley 34 includes framework platform 344 and support frame 343, and framework platform 344 is rectangle frame structure, frame
It is arranged that there are two for placing the storage position 345 of filter column 32, be provided with and 321 middle part of column shell in storage position 345 on platform 344
The locating slot 346 that the ears or side handles of a utensil 324 are adapted to, the four corners of framework platform 344 and four support frames 343 vertically connect, four supports
Frame 343 is respectively arranged with lifting or declines the electric cylinder 342 of framework platform 344, and the foot of support frame 343 is provided with castor 341.
When being replaced to filter column 32, spare filter column is placed on the off-duty storage position 345 of cross traveling trolley 34;Firstly, by electronic
Cylinder 342 declines framework platform 344, sliding cross traveling trolley 34 make locating slot 346 be in the ears or side handles of a utensil 324 in the middle part of filter column 32 just under
Side;Secondly, being lifted framework platform 344 by electric cylinder 342, fall into the ears or side handles of a utensil 324 in locating slot 346, it is flat to continue lifting frame
344 a small distance of platform makes cross traveling trolley 34 support the weight of filter column 32;Then, dismantle top cover 31, filter column 32 and bottom cover 33 it
Between bolt connection can remove filter column 32, top cover 31, filter column 32 and bottom cover 33 are cleared up, ensure that the filtering of filter column 32
Space avoids the obstruction of some bypass lines;Finally, driving cross traveling trolley 34 is mobile, filter column 32 is made to return to top cover 31 and bottom
Between lid 33, top cover 31, filter column 32 and bottom cover 33 are bolted, that is, complete back dress;Or spare filter column is made to move to top cover 31
Between bottom cover 33, top cover 31, spare filter column and bottom cover 33 are bolted, that is, complete the replacement of filter column 32.
Column shell 321 uses glass steel material, observes internal service condition convenient for people;The top of column shell 321 is provided with excessive
Waterpipe 325, for 32 water level inside of filter column excessively high water or backwashing water to be discharged.The other end and water of overflow pipe 325
Case 7 connects, and spilling water ball valve 326 is provided on overflow pipe 325, and water tank 7 is for collecting water in backwashing water and filter column 32
Underground water when position is excessively high contains some iron-oxidizing bacterias and manganese oxidizing bacteria in backwashing water, contains ferrous iron and two in underground water
Valence manganese;Therefore, life and the breeding environment that can provide iron-oxidizing bacteria and manganese oxidizing bacteria in water tank 7, after a period of time, can deposit
The water surface of water tank 7 forms colloid substance, as iron-oxidizing bacteria and manganese oxidizing bacteria;This colloid substance is periodically passed through into blowing
Mouth 316 is added in filter column 32, and the filter effect of microbial deactivation apparatus 3 can be improved.31 top of top cover is provided with air vent
313,313 upper end of air vent is furnished with movable port lid 314, and when filter air pressure inside is greater than external atmosphere pressure, port lid 314 will
It is washed open by the gas of filter interior, to discharge gas excessive in filter, to guarantee that filter inner and outer air pressure is consistent;Instead
It, port lid 314 will be in closed state, to prevent some sundries from falling into filter.
Utilize the filter method of above-mentioned underground water deferrization and demanganization device, comprising the following steps: underground water passes through the first diving
Pump 1 is extracted in aeration tank 2, after the weak aeration in aeration tank 2, so that the dissolved oxygen in underground water reaches 4-6mg/L;Again will
Underground water after weak aeration is transported to microbial deactivation apparatus 3, filtering velocity 5-7m/h, ferrous iron and bivalent manganese meeting in underground water
The iron-oxidizing bacteria and manganese oxidizing bacteria being attached on filtrate 322 are oxidized into ferric iron and manganic, thus by 322 institute of filtrate
It intercepts;Domestic water standard has been had reached through the filtered underground water of microbial deactivation apparatus 3, has partially been lauched and is passed through instead
Spare in flushing tank 5, remaining underground water is then passed through in clear water reserviors 4 as domestic water or industrial water;Work as microbe filter
The filtration time of device 3 reaches 48 hours, needs that the water in the wash pool 5 that recoils is passed through microbe filter by the second immersible pump 52
It is backwashed in device 3, backwashing time is 3 minutes, and back washing strength is 10L/ (sm2), to rinse out on filtrate 322
The ferriferous oxide and Mn oxide of attachment, and flowed into water tank 7 by overflow pipe 325.
Finally, it should be noted that the above embodiments are merely illustrative of the technical solutions of the present invention, rather than its limitations;Although
Present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should understand that: it is still
It is possible to modify the technical solutions described in the foregoing embodiments, or some or all of the technical features is carried out
Equivalent replacement;And these are modified or replaceed, it does not separate the essence of the corresponding technical solution various embodiments of the present invention technical side
The range of case should all cover within the scope of the claims and the description of the invention.
Claims (9)
1. a kind of facility for iron and manganese removal based on microorganism, it is characterised in that: including the first immersible pump, aeration tank, microorganism mistake
Filter device, the second immersible pump, recoil wash pool, clear water reserviors, water tank and aerator;It is arranged between the aeration tank and missile silo
Have the first immersible pump, aeration tank equipped with aerator, aerator include by aerated conduit connect air pressure pump and
Aeration plate is provided with flowmeter on aerated conduit, and aeration plate is located at the top of aeration tank, and the upper end of aeration plate is provided with lifting dress
It sets, and has been evenly arranged equidistant exhaust pipe on aeration plate, equidistant gas vent has been evenly arranged on exhaust pipe;It is described
Aeration tank and microbial deactivation apparatus are linked in sequence, the lower end of microbial deactivation apparatus be provided with outlet threeway respectively with backwash
Pond is connected with clear water reserviors, is provided with the second immersible pump between the wash pool that recoils and outlet threeway;The microbial deactivation apparatus includes
Top cover, filter column, bottom cover and cross traveling trolley, top cover, filter column and bottom cover connect from top to bottom, and to be detachably connected, cross traveling trolley is used
In support filter column;The water tank is connect with the overflow pipe on filter column top;The top cover upper end is provided with water inlet pipe, enters water
Pipeline is connected with the spray equipment inside top cover;The filter column includes column shell, filtrate and bottom plate, the top setting of the column shell
There is overflow pipe, the ears or side handles of a utensil are provided in the middle part of column shell, bottom plate is in cellular, is arranged in the lower end of column shell, the aperture on bottom plate is
0.3-0.5mm;The filtrate is microorganism carrier, and filtrate includes bed course and filter layer, and filter layer, bed course and bottom plate are in filter housing
In in up and down arrangement;The lower end of the bottom cover is provided with outlet threeway and foot prop;The cross traveling trolley includes framework platform and branch
Support, framework platform are rectangle frame structure, and there are two the storage position for placing filter column, storage positions for setting on framework platform
On be provided with the locating slot being adapted to the ears or side handles of a utensil in the middle part of column shell, the four corners of framework platform and four support frames vertically connect,
Four support frames are respectively arranged with lifting or decline the electric cylinder of framework platform, and the foot of support frame is provided with castor.
2. as described in claim 1 based on the facility for iron and manganese removal of microorganism, it is characterised in that: the aeration tank is using weak quick-fried
Gas, the concentration of the dissolved oxygen after aeration in water are 4-6mg/L.
3. as described in claim 1 based on the facility for iron and manganese removal of microorganism, it is characterised in that: the top cover top is provided with
Air vent and drain hole, air vent upper end are provided with movable port lid.
4. as described in claim 1 based on the facility for iron and manganese removal of microorganism, it is characterised in that: the microbial deactivation apparatus
Outlet threeway and the second immersible pump and clear water reserviors between be respectively arranged with backwash ball valve and clear water reserviors ball valve.
5. as described in claim 1 based on the facility for iron and manganese removal of microorganism, it is characterised in that: the filter layer of the filtrate from
Under it is supreme be sequentially arranged quartz sand, manganese sand and active carbon particle, the partial size of quartz sand, manganese sand and active carbon particle is 0.6-
1.5mm, the mass ratio of quartz sand, manganese sand and active carbon particle are 5:3:2.
6. as described in claim 1 based on the facility for iron and manganese removal of microorganism, it is characterised in that: the top cover and bottom cover and filter
It is provided with sealing ring between column, is provided with Inlet ball valve on water inlet pipe.
7. as described in claim 1 based on the facility for iron and manganese removal of microorganism, it is characterised in that: the column shell uses glass reinforced plastic
Material, top cover and bottom cover use stainless steel.
8. a kind of microbe filter method using the facility for iron and manganese removal described in claim 1 based on microorganism, feature
It is, comprising the following steps: underground water is extracted in aeration tank by the first immersible pump, after the weak aeration in aeration tank, is made
The dissolved oxygen obtained in underground water reaches 4-6mg/L;The underground water after weak aeration is transported to microbial deactivation apparatus again, filtering velocity is
5-7m/h, the iron-oxidizing bacteria and manganese oxidizing bacteria that ferrous iron and bivalent manganese in underground water can be attached on filtrate are oxidized into
Ferric iron and manganic, to be intercepted by filtrate;Life has been had reached through the filtered underground water of microbial deactivation apparatus
Water supply standard, be partially lauched be passed through recoil wash pool in it is spare, remaining underground water be then passed through in clear water reserviors as life use
Water or industrial water;When the filtration time of microbial deactivation apparatus reach 24-48 it is small when, need by the second immersible pump will recoil
Water in wash pool, which is passed through in microbial deactivation apparatus, to be backwashed, and backwashing time is 3-5 minutes, back washing strength 7-
11L/(s·m2), to rinse out the ferriferous oxide and Mn oxide that adhere on filtrate, and water tank is flowed by overflow pipe
In.
9. microbe filter method as claimed in claim 8, it is characterised in that: contain in the backwashing water that the water tank is collected
There are iron-oxidizing bacteria and manganese oxidizing bacteria, water tank is flowed by overflow pipe when the water level of underground water is excessively high in filter column, in underground water
The ferrous iron and bivalent manganese contained provides the environment of life and breeding for the iron-oxidizing bacteria and manganese oxidizing bacteria of water tank;After 3-6 days,
Iron-oxidizing bacteria and manganese oxidizing bacteria can form colloid substance in the water surface of water tank;Periodically this mucilage binding substance is passed through on top cover
The drain hole at end is added in filter column.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610771556.XA CN106365295B (en) | 2016-08-30 | 2016-08-30 | Facility for iron and manganese removal and microbe filter method based on microorganism |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610771556.XA CN106365295B (en) | 2016-08-30 | 2016-08-30 | Facility for iron and manganese removal and microbe filter method based on microorganism |
Publications (2)
Publication Number | Publication Date |
---|---|
CN106365295A CN106365295A (en) | 2017-02-01 |
CN106365295B true CN106365295B (en) | 2019-08-02 |
Family
ID=57902193
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610771556.XA Active CN106365295B (en) | 2016-08-30 | 2016-08-30 | Facility for iron and manganese removal and microbe filter method based on microorganism |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106365295B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108178357A (en) * | 2018-02-06 | 2018-06-19 | 田静 | A kind of comprehensive water environment pollution prevention system |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1733618A (en) * | 2005-07-27 | 2006-02-15 | 东华大学 | Process and apparatus for removing ferromanganese from underground water |
CN103486111A (en) * | 2013-09-24 | 2014-01-01 | 天津中联精密铸造有限公司 | Movable oil filtering device |
CN104108838A (en) * | 2014-08-06 | 2014-10-22 | 农业部环境保护科研监测所 | Method for removing iron and manganese from rural underground drinking water |
-
2016
- 2016-08-30 CN CN201610771556.XA patent/CN106365295B/en active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1733618A (en) * | 2005-07-27 | 2006-02-15 | 东华大学 | Process and apparatus for removing ferromanganese from underground water |
CN103486111A (en) * | 2013-09-24 | 2014-01-01 | 天津中联精密铸造有限公司 | Movable oil filtering device |
CN104108838A (en) * | 2014-08-06 | 2014-10-22 | 农业部环境保护科研监测所 | Method for removing iron and manganese from rural underground drinking water |
Also Published As
Publication number | Publication date |
---|---|
CN106365295A (en) | 2017-02-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105523644B (en) | A kind of integrated treatment unit and method of the high ammonia nitrogen underground water of high-iron and high manganese | |
CN106365295B (en) | Facility for iron and manganese removal and microbe filter method based on microorganism | |
CN204803432U (en) | Take circulating filter apparatus's plating bath | |
CN204310862U (en) | Removing of iron and manganese refining plant | |
CN106242184B (en) | Underground water deferrization and demanganization device | |
CN204958594U (en) | Mobile device that laboratory liquid water disposal retrieved | |
CN205974201U (en) | Groundwater iron and manganese removal device | |
CN208791441U (en) | A kind of equipment for processing industrial sewage of high-efficiency environment friendly | |
CN106745683A (en) | A kind of modularization biofiltration case | |
CN206278983U (en) | A kind of controllable biotechnology effluent treatment plant | |
CN206433597U (en) | A kind of fishpond oxygenation decontamination system | |
CN205455390U (en) | Drench recirculating aquaculture device | |
CN106242183B (en) | Can microorganisms online underground water deferrization and demanganization device and filter method | |
CN205933435U (en) | A intelligent water purifier for food processing | |
CN208776382U (en) | A kind of catalytic ozonation container integrated apparatus | |
CN208814748U (en) | Combined integral membrane bioreactor | |
CN208883590U (en) | A kind of small ship type sedimentation tank device for treating sewage | |
CN107162268A (en) | A kind of processing unit of leather-making waste water | |
CN208802969U (en) | A kind of processing system proposing mark transformation for sewage treatment plant tail water | |
CN202449954U (en) | Ecological circulating filtration biological island | |
CN107777775B (en) | Sewage treatment system with nitrogen and phosphorus removal function | |
CN206408046U (en) | A kind of processing system | |
CN206051801U (en) | A kind of transportable water treatment apparatus | |
CN206033480U (en) | Biological treatment system of scenic water | |
CN109264855A (en) | Rotating excitation field-membrane bioreactor combines vessel oily water processing method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |