CN2034972U - Iron and manganese removing device for groundwater - Google Patents
Iron and manganese removing device for groundwater Download PDFInfo
- Publication number
- CN2034972U CN2034972U CN88203110U CN88203110U CN2034972U CN 2034972 U CN2034972 U CN 2034972U CN 88203110 U CN88203110 U CN 88203110U CN 88203110 U CN88203110 U CN 88203110U CN 2034972 U CN2034972 U CN 2034972U
- Authority
- CN
- China
- Prior art keywords
- water
- pipe
- filter
- iron
- utility
- 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.)
- Withdrawn
Links
Images
Classifications
-
- 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
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model, relating to an iron and manganese removing device for groundwater, belongs to water-treating equipment, and is composed of a deep-well pump, an aerator, a reaction tank, a booster pump, a filter, and a backwashing distributing pipe. The utility model is characterized in that the aerator is a tubular body, and an aeration adjusting valve is equipped on the tubular body; the filter is a bio-filter, and a biochemistry film is arranged on the filtering material; the backwashing distributing pipe is equipped with a bore to form a high resisting and backwashing distribution system. The utility model has the advantages of simple structure, less investment, and stable effects of water treatment and it can reduce energy consumption and has excellent removal effect on micro-pollutant in underground water, such as ammonia nitrogen and bacteria.
Description
This equipment belongs to water treating equipment, particularly phreatic equipment of removing iron and manganese.
Contain excessive iron, manganese in the water, not only directly influence HUMAN HEALTH, and have a strong impact on industrial production, thus remove the excessive iron that contains in the water, the technology of manganese has just grown up, and the equipment of deferrization and demanganization occurred mutually suitablely.Is the equipment of basis at present with the aeration contact oxidation method, be with natural manganese sand as filtration medium, utilize airborne oxygen underground water to be undertaken by force by aeration tower as oxygenant
Gas, carbonic acid gas in the water that sheds increases the dissolved oxygen in the water, and improve pH value in the water as far as possible, this just needs big volumetrical reaction tank, and water enters in the filtering basin then, and the low price iron in the water, manganese are held back removal attached to the filter tank filter material surface by filtrate after being oxidized to high price iron, manganese gradually.When iron in the water, when manganese content is high, need TSA, twice compressive reaction and filtration, make equipment huge, energy consumption is excessive.
The purpose of this utility model is to provide underground water deferrization, the demanganization equipment that equipment is simple, power consumption is low.
The utility model is according to the technical project that is referred to as " biological filter process ".The F that utilizes in the underground water to be contained
e , M
n 
, NH
3-N, CO
2, in the filter tank, cultivate iron bacteria, and make on its filtrate that anchors at the filter tank rapidly.Because iron bacteria is chemoautotrophic bacteria, it must a large amount of iron of oxidation, and manganese and obtain energy is simultaneously again with CO
2Be carbon source, with the inorganic nitrogen is nitrogenous source, underground water provides good growth and breeding environment for iron bacteria, make the filter tank form the biological filter soon, iron, manganese are high price iron, manganic compound by the enzymatic oxidation that iron bacteria produced soon so at a low price, and absorption is trapped in the filter tank by bacterium excretory mucus; The meta-bolites of iron bacteria has very strong katalysis again simultaneously, can quicken the oxidation of iron in the water, manganese, under above-mentioned biochemical action, formed a kind of complex chemical compound and accumulated on the filtrate, thereby reached the purpose of removing iron in the water, manganese effectively.
The purpose of this utility model is to realize like this, former water is extracted out through aerator realization aeration, make the water thorough mixing through reaction tank again, enter to filter in the biological filter through pressurization again and remove iron, manganese, obtain qualified processed water, for guaranteeing deironing, manganese effect, carry out back flushing to the biological filter by the back flushing water distributing pipe.
The utility model has removed strong aeration set in the former aeration contact oxidation method and the strong structures that react, and replace the aerator and the small-sized reaction tank of similar pipe fitting, facility investment and the consumption that reduces the energy have been saved, biological filter filter process effect stability, it not only has excessive iron, manganese effect in the good removal water, and phreatic micro polluting substance such as ammonia nitrogen, bacterium are also had good removal effect.It is calculated that with result on trial to show that an engineering initial cost of water treatment capacity Q=1000 ton per day is 4.5 ten thousand yuan, the investment of ton water conservancy project journey is 45 yuan/day.
Concrete structure of the present utility model is provided by embodiment and accompanying drawing.
The underground water deferrization manganese equipment block scheme that Fig. 1 the utility model proposes for foundation.
Fig. 2 is the structural representation according to the aerator that the utility model proposes.
The structure of filter synoptic diagram that Fig. 3 the utility model proposes for foundation.
Describe the underground water deferrization and demanganization equipment that forms according to the utility model in detail below in conjunction with embodiment and accompanying drawing.
Former water is entered aerator (2) aeration by drowned pump (1) extraction, aeration process only needs weak aeration, its required dissolved oxygen is 4-5mg/L, this has just determined that aerator is simple, the only similar pipe fitting of this aerator, the gangway (7,8) of water and gas inlet (10), aerating regulation valve (9) are arranged on it, can carry out the adjusting of aeration rate according to required aeration intensity; Enter reaction tank (3) reaction from the effusive water of aerator, the reaction times is 10-15 minute, and water residence time in reaction tank shortens, and makes that the volume of reaction tank is little, and reaction tank can adopt steel plate or plastic plate to manufacture.By force (forcing) pump (4) pressurization water is delivered in the strainer (5) again and filters, this strainer is a biological filter tank, and this strainer is made up of bearing (11), end socket (12), cylindrical shell (13), water inlet pipe and water outlet pipe (14,15) vapor pipes (16), filter material layer (17), bed course (18), biochemical film (21), Inlet and outlet water valve (19,20).Filter material layer, bed course are filled in the cylindrical shell bottom, and bed course is made up of three layers of cobble, one deck manganese sand, and particle diameter is respectively 32-16,16-8,8-4,4-2mm, and bed thickness is respectively 150,100,100,100mm; Filtrate is made up of manganese sand on bed course top, and the manganese sand grains directly is 0.6-1.43mm, bed thickness is 700-800mm, filtrate outside is surrounded by biochemical film, and this biochemistry film is to cultivate iron bacteria to contain iron, manganese, ammonia nitrogen, carbonic acid gas in the water, makes it anchor at that filter material surface forms; This film iron, the synthetic high price of manganese iron, manganic compound at a low price is trapped in the filter tank, and the ripening stage of this film is 28-32 days.Cylindrical shell is a steel pressure formula container, and water inlet pipe is from end socket feeds cylindrical shell, and rising pipe is surveyed under cylindrical shell, and the Inlet and outlet water valve is positioned on respectively on the water inlet pipe and water outlet pipe, and vapor pipe is positioned on the transverse tube of water inlet pipe, water with 8-20 rice/hour filtering velocity flow out through filter.For guaranteeing the deferrization and demanganization effect, the utility model also is furnished with back flushing water distributing pipe (6) strainer is regularly carried out back flushing, and wash out the material that is trapped in the strainer, the back flushing water distributing pipe is installed in the bottom of filter cylinder, its water inlet pipe (22) is an one with the rising pipe (15) of strainer, have hole (25) on the back flushing water distributing pipe, form big resistance back flushing water distribution system, it passes the bed course of strainer, its water shoot (23) is positioned at the filter inleting pipe lower end, is equipped with water discharging valve (24) on the water shoot.
The utility model is widely used in the processing of vast rural area and township enterprise's drinking water and water for industrial use.
Claims (1)
1, a kind of underground water deferrization, demanganization equipment are made of drowned pump [1], reaction tank [3], force (forcing) pump [4], aerator [2], it is characterized in that:
It also comprises strainer [5] in constituting, strainer is by bearing [11], end socket [12], cylindrical shell [13], water inlet pipe and water outlet pipe [14,15], vapor pipe [16] filter material layer [17], bed course [18], Inlet and outlet water valve [19,20] back flushing water distributing pipes [6] constitute, bed course, filter material layer, the filter material layer outside surface biochemical film [21] of growing is housed in the cylindrical shell, water inlet pipe mouth is positioned at the centre of cylindrical shell top end socket, vapor pipe is positioned on the water inlet pipe, and inlet valve is positioned on the water inlet pipe, and flowing water Valve is positioned on the rising pipe; Back flushing water distributing pipe [6] is positioned at the filter cylinder bottom, pass bed course, its water inlet pipe [22] is an one with filter outlet pipe [15], and water shoot [23] is positioned at the filter inleting pipe lower end, be equipped with water discharging valve [24] on the water shoot, have hole [25] on the back flushing water distributing pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN88203110U CN2034972U (en) | 1988-02-11 | 1988-02-11 | Iron and manganese removing device for groundwater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN88203110U CN2034972U (en) | 1988-02-11 | 1988-02-11 | Iron and manganese removing device for groundwater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2034972U true CN2034972U (en) | 1989-03-29 |
Family
ID=4837995
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN88203110U Withdrawn CN2034972U (en) | 1988-02-11 | 1988-02-11 | Iron and manganese removing device for groundwater |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2034972U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1309664C (en) * | 2004-12-30 | 2007-04-11 | 西安建筑科技大学 | Reinforced biological contacting oxidation water correction apparatus |
| CN102603080A (en) * | 2012-03-23 | 2012-07-25 | 北京工业大学 | Rapid starting method for high-iron and manganese underground water biological purification filtering layer |
| CN110723840A (en) * | 2019-11-20 | 2020-01-24 | 华电水务科技股份有限公司 | Method and device for removing iron and manganese in underground water |
-
1988
- 1988-02-11 CN CN88203110U patent/CN2034972U/en not_active Withdrawn
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1309664C (en) * | 2004-12-30 | 2007-04-11 | 西安建筑科技大学 | Reinforced biological contacting oxidation water correction apparatus |
| CN102603080A (en) * | 2012-03-23 | 2012-07-25 | 北京工业大学 | Rapid starting method for high-iron and manganese underground water biological purification filtering layer |
| CN102603080B (en) * | 2012-03-23 | 2013-07-10 | 北京工业大学 | Rapid starting method for high-iron and manganese underground water biological purification filtering layer |
| CN110723840A (en) * | 2019-11-20 | 2020-01-24 | 华电水务科技股份有限公司 | Method and device for removing iron and manganese in underground water |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103663725B (en) | Based on Continuous Flow biological denitrification method and the device of granule sludge | |
| US4009099A (en) | Apparatus and process for removing ammonia nitrogen from waste water | |
| CA1307059C (en) | Method of treating waste water and equipment therefor | |
| CN101302069B (en) | Technological system and method for removing carbon, nitrogen and sulphur in waste water synchronously | |
| CN108217964A (en) | A kind of sewage water advanced treatment apparatus and method | |
| CN105366891A (en) | Treatment method of livestock culture wastewater | |
| CN110217890A (en) | Strengthen the device and method of water body nitrogen removal based on aerobic denitrification fungi | |
| CN206886902U (en) | A kind of biological cycle method sewage disposal system | |
| CN201990579U (en) | Bilayer biology-sand filter | |
| CN100519449C (en) | Quick-decomposing biological sewage treatment method and treating system | |
| CN107162315A (en) | Biological cycle method sewage disposal system | |
| CA1057430A (en) | Apparatus and process for removing ammonia nitrogen from waste water | |
| CN103043860B (en) | Leachate utilizing equipment and method in biomass landfilling process | |
| CN209974541U (en) | Sewage treatment device | |
| CN2034972U (en) | Iron and manganese removing device for groundwater | |
| CN105314802A (en) | Livestock and poultry breeding wastewater treatment system | |
| CN109502928A (en) | Rain dirt mixing water, black and odorous water governing system | |
| CN211644787U (en) | New rural domestic sewage anaerobic wetland ecological purification system | |
| CN2432208Y (en) | Glazed sphere filling material for treating water | |
| CN209412043U (en) | Rain dirt mixing water, black and odorous water governing system | |
| CN209618991U (en) | A kind of denitrification deep-bed filter structure applied to sewage treatment plant's advanced treating | |
| CN104961288B (en) | The sewage disposal system that ecological oxidation ditch is combined with ecological box wetland | |
| CN113264586A (en) | MBR (membrane bioreactor) process for treating nitrate wastewater | |
| CN207175701U (en) | A kind of livestock breeding wastewater integrated treatment unit | |
| CN209143973U (en) | Integral domestic sewage treatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| 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 |