CN205635277U - Integration removes ferro -manganese equipment - Google Patents
Integration removes ferro -manganese equipment Download PDFInfo
- Publication number
- CN205635277U CN205635277U CN201620459088.8U CN201620459088U CN205635277U CN 205635277 U CN205635277 U CN 205635277U CN 201620459088 U CN201620459088 U CN 201620459088U CN 205635277 U CN205635277 U CN 205635277U
- Authority
- CN
- China
- Prior art keywords
- siphon
- tube
- pipe
- aeration
- filter tank
- 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
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model discloses an integration removes ferro -manganese equipment, including oxidation reaction district and automatic filtration backwash district, the oxidation reaction district includes: the perforated aeration tube of aeration oxidation pond, water inlet, water inlet top, the filler ball of aeration oxidation pond inside and sieve tray, the left first inspection manhole of oxidation pond, automatic filtration backwash district includes: the filter plate and the pan of bottom in filtering pond, the filtering pond, the last water hole in the three -way pipe at pan top, the U type water seal pipe of connecting three -way pipe and aeration oxidation pond, filtering pond four corners, the delivery port at filtering pond top, the siphon of connecting the three -way pipe, the siphon downtake of connecting the siphon and siphon auxiliary tube and siphon tube, connection siphon auxiliary tube and siphon tube's exhaust tube, at the pumping shaft on the terminal siphon breaking fill of siphon tube, filtering pond side and exhaust -valve, second inspection manhole. The problem of prior art is solved, it is low not only to take up an area of little, energy consumption, can reach higher treatment effect moreover, easy and simple to handle efficient, easy implementation.
Description
Technical field
This utility model belongs to water treatment facilities, is specifically related to a kind of integration ferrum-manganese removing device.
Background technology
The general water quality of subsoil water is preferable, generally pays the utmost attention to as life, the water source of industrial water, but I
In state's much area subsoil water, content of iron and manganese exceeds standard, and when serving not only as domestic water, impact is checked colors, taste, smelt
Deng the requirement of organoleptic indicator, also can produce spot on apparatus, washings, as also can be right during industrial water
Papermaking, weave, print and dye, the numerous industry of chemical industry, leather has undesirable effect, therefore, when with iron content, manganese
Subsoil water as water source time, it is necessary to carry out deferrization and demanganization process, although at present removing of iron and manganese technique the most on the market
Maturation, but backwash must rely on booster pump to realize, and energy consumption is higher, and takes up an area big, and operation is complicated loaded down with trivial details.
Utility model content
The purpose of this utility model is to provide a kind of integration ferrum-manganese removing device, not only takes up an area little, energy consumption
Low, and higher treatment effect can be reached, efficiency easy and simple to handle is high, easily implements.
For reaching above-mentioned purpose, major technique solution of the present utility model is to provide a kind of integration except ferrum
Manganese equipment, including oxidation reaction zone and automatic fitration backwash district, oxidation reaction zone includes: aeration oxidation pool,
It is arranged on the water inlet of aeration oxidation pool left bottom, is arranged on bottom aeration oxidation pool inwall above water inlet
Boring aeration pipe, be arranged on the filling ball within aeration oxidation pool, be arranged on the right side of aeration oxidation pool inwall
Sieve tray, be arranged on the first inspection manhole on the left of aeration oxidation pool, automatic fitration backwash district includes: filter
Pan above pond, the filter plate being arranged on filter tank inner bottom part and filter plate, be arranged on pan top tee T,
The connecting tee tube side mouth of pipe and the U-shaped water sealing (sealing water) pipe at aeration oxidation pool top, be arranged on corner, filter tank upper water hole,
The outlet being arranged on top, filter tank, the siphon being connected to tee T upper orifice, the connection right mouth of pipe of siphon
Siphon down-comer, the auxiliary siphon tube being connected on siphon, be connected to the siphon destructive on the right side of siphon
Pipe, connect auxiliary siphon tube and the exhaust tube of siphon destructing tube, be in the siphon destructive of siphon destructing tube end
Bucket, it is arranged on the gully on the right side of filter tank, is arranged on filter tank and the exhaust-valve of gully midfeather, is arranged on
Second inspection manhole of filter tank outer wall.
Described pan top is pyramid type.
The described water level in gully is higher than the siphon down-comer lower end mouth of pipe.
Described siphon connects the side of siphon down-comer higher than connecting tee pipe side.
Less than bottom filter tank bottom described gully.
10 to 15 centimeters of spaces are left bottom described filter plate and filter tank.
The beneficial effects of the utility model are: not only integrated degree is high, and floor space is little, and observes
Liquid level is convenient, and operation is convenient, and pretreatment is more thorough.
Accompanying drawing explanation
Fig. 1 be this utility model one embodiment face structural representation,
Fig. 2 is the plan structure schematic diagram of this utility model one embodiment,
In figure: 1. aeration oxidation pool, 2. water inlet, 3. boring aeration pipe, 4. filling ball, 5. sieve tray,
6. the first inspection manhole, 7.U type water sealing (sealing water) pipe, 8. pan, 9. tee T, 10. go up water hole, 11. outlets,
12. siphons, 13. siphon down-comers, 14. auxiliary siphon tubes, 15. siphon destructing tubes, 16. exhaust tubes, 17.
Siphon destructive bucket, 18. gullys, 19. exhaust-valves, 20. second inspection manholes, 21. filter plates, 22. filter tanks.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, to the technology in this utility model embodiment
Scheme is clearly and completely described, it is clear that described embodiment is only this utility model part
Embodiment rather than whole embodiments.Based on the embodiment in this utility model, ordinary skill
The every other embodiment that personnel are obtained under not making creative work premise, broadly falls into this practicality new
The scope of type protection.
As shown in Figure 1 and Figure 2, this utility model provides a kind of integration ferrum-manganese removing device, including oxidation
Reaction zone and automatic fitration backwash district, oxidation reaction zone includes: aeration oxidation pool 1, be arranged on aeration oxidation pool
The water inlet 2 of 1 left bottom, it is arranged on the boring aeration above water inlet 2 bottom aeration oxidation pool 1 inwall
Pipe 3, it is arranged on the filling ball 4 within aeration oxidation pool 1, is arranged on the sieve on the right side of aeration oxidation pool 1 inwall
Orifice plate 5, being arranged on the first inspection manhole 6 on the left of aeration oxidation pool 1, automatic fitration backwash district includes: filter
Pan 8 above pond 22, the filter plate 21 being arranged on filter tank 22 inner bottom part and filter plate 21, is arranged on pan 8
The tee T 9 at top, connecting tee pipe 9 side pipe mouth and the U-shaped water sealing (sealing water) pipe 7 at aeration oxidation pool 1 top, set
Put 22 4 jiaos of filter tank upper water hole 10, be arranged on the outlet 11 at top, filter tank 22, be connected to tee T
The siphon 12 of 9 upper orifices, connect the siphon down-comer 13 of the right mouth of pipe of siphon 12, be connected to siphon
Auxiliary siphon tube 14 on 12, it is connected to the siphon destructing tube 15 on the right side of siphon 12, connects siphon auxiliary
The exhaust tube 16 of pipe 14 and siphon destructing tube 15, be in siphon destructing tube 15 end siphon destructive bucket 17,
It is arranged on the gully 18 on the right side of filter tank 22, is arranged on filter tank 22 and the exhaust-valve of gully 18 midfeather
19, the second inspection manhole 20 of filter tank 22 outer wall it is arranged on.
Described pan 8 top is pyramid type.
The described water level in gully 18 is higher than the siphon down-comer 13 lower end mouth of pipe.
Described siphon 12 connects the side of siphon down-comer 13 higher than connecting tee pipe 9 side.
Less than bottom filter tank 22 bottom described gully 18.
During integration ferrum-manganese removing device work described in the utility model, first start boring aeration pipe 3 right
Aeration oxidation pool 1 carries out aeration, promotes oxygen content, subsoil water is then pumped into aeration oxidation pool 1, oxygen
Changing the filling ball 4 in pond can make oxygen contact more fully with subsoil water, the ferrous ion in subsoil water and manganese
Ion is oxidized to ferric iron, tetravalent manganese, the subsoil water after peroxidating in the case of oxygen is abundant respectively
Through sieve tray 5, entering automatic fitration backwash district from U-shaped water sealing (sealing water) pipe 7 again, tetravalent manganese is with ferric precipitation
The manganese sand filtering material that thing is placed in pan 8 when pan 8 adsorbs and retains, thus reaches to solve underground
The problem that water ferrimanganic exceeds standard, gradually increases accumulation along with sedimentary in pan 8, and the filtering velocity in filter tank 22 is gradually
Reducing, after the water logging in filter tank 22 there has not been siphon destructive bucket 17, the subsoil water after Partial filtration is via siphon
Pipe 12 flows upwards out, and when flowing through the peak of siphon 12, inner air tube is instantaneous to be discharged, then via
Siphon down-comer 13 flows out outward, and the water in pan 8 also leads to siphon 12 along three and flows up simultaneously,
Thus the attachment on filtrate is rinsed, until siphon destructive bucket 17 spills the water surface, air enters,
Stopping backwash, so far an automatic fitration process completes, and whole process is without additionally increasing power, it is not necessary to
Opening and closing valve, simple to operate, it is simple to management.
Claims (5)
1. an integrated ferrum-manganese removing device, by aeration oxidation pool (1), is arranged on aeration oxidation pool (1) left side
The water inlet (2) of bottom, it is arranged on the perforation of the top of water inlet (2) bottom aeration oxidation pool (1) inwall
Aeration tube (3), it is arranged on the internal filling ball (4) of aeration oxidation pool (1), is arranged on aeration oxidation pool
(1) sieve tray (5) on the right side of inwall, be arranged on first inspection manhole (6) in aeration oxidation pool (1) left side
Constitute, it is characterised in that be additionally provided with automatic fitration backwash district, including: filter tank (22), be arranged on filter
The filter plate (21) of pond (22) inner bottom part and the pan (8) of filter plate (21) top, be arranged on pan (8)
The tee T (9) at top, connecting tee pipe (9) side pipe mouth and the U-shaped water at aeration oxidation pool (1) top
Tube sealing (7), it is arranged on the upper water hole (10) of filter tank (22) corner, is arranged on filter tank (22) top
Outlet (11), be connected to tee T (9) upper orifice siphon (12), connect siphon (12)
The siphon down-comer (13) of the right mouth of pipe, the auxiliary siphon tube (14) being connected on siphon (12), company
It is connected on the siphon destructing tube (15) on siphon (12) right side, connection auxiliary siphon tube (14) and siphon to break
The exhaust tube (16) of bad pipe (15), be in siphon destructing tube (15) end siphon destructive bucket (17),
It is arranged on the gully (18) on right side, filter tank (22), is arranged in filter tank (22) and gully (18)
The exhaust-valve (19) of partition, it is arranged on second inspection manhole (20) of filter tank (22) outer wall.
A kind of integration ferrum-manganese removing device the most according to claim 1, it is characterised in that described pan (8)
Top is pyramid type.
A kind of integration ferrum-manganese removing device the most according to claim 1, it is characterised in that described gully (18)
Interior water level is higher than siphon down-comer (13) the lower end mouth of pipe.
A kind of integration ferrum-manganese removing device the most according to claim 1, it is characterised in that described siphon (12)
Connect the side of siphon down-comer (13) higher than connecting tee pipe (9) side.
A kind of integration ferrum-manganese removing device the most according to claim 1, it is characterised in that described gully (18)
Bottom is less than bottom, filter tank (22).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620459088.8U CN205635277U (en) | 2016-05-18 | 2016-05-18 | Integration removes ferro -manganese equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620459088.8U CN205635277U (en) | 2016-05-18 | 2016-05-18 | Integration removes ferro -manganese equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205635277U true CN205635277U (en) | 2016-10-12 |
Family
ID=57056684
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620459088.8U Active CN205635277U (en) | 2016-05-18 | 2016-05-18 | Integration removes ferro -manganese equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205635277U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109354196A (en) * | 2018-11-16 | 2019-02-19 | 安徽国祯环境修复股份有限公司 | A kind of artificial swamp for same for treating acidic mine wastewater |
| CN110559864A (en) * | 2019-09-23 | 2019-12-13 | 苏州苏科环保科技有限公司 | ultrafiltration membrane self-cleaning device |
-
2016
- 2016-05-18 CN CN201620459088.8U patent/CN205635277U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109354196A (en) * | 2018-11-16 | 2019-02-19 | 安徽国祯环境修复股份有限公司 | A kind of artificial swamp for same for treating acidic mine wastewater |
| CN110559864A (en) * | 2019-09-23 | 2019-12-13 | 苏州苏科环保科技有限公司 | ultrafiltration membrane self-cleaning device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107117752A (en) | A kind of sewage treating and recovering device | |
| CN205907131U (en) | Domestic sewage treatment device | |
| CN205635277U (en) | Integration removes ferro -manganese equipment | |
| CN208493431U (en) | Mixing wastewater with air backwash automatic cleaning lamination filter | |
| JP2017536234A (en) | Water purification apparatus and water filtration method using the water purification apparatus | |
| CN107915309A (en) | A kind of method that fine catalyst efficiently separates simultaneously automatic cycle during catalytic oxidation treatment sewage | |
| CN207727673U (en) | A kind of secondary water-supply cistern | |
| CN212356790U (en) | Filtering device for treating lead-acid wastewater | |
| CN212524688U (en) | Two filtration circulation basin spraying cabinets | |
| CN203754484U (en) | Novel efficient iron-and-manganese removal filter device | |
| CN208327538U (en) | A kind of city river sewage-treatment plant | |
| CN208809806U (en) | A kind of intelligence ultrafilter | |
| CN202355882U (en) | Improved structure for by-pass filtration device of circulating water | |
| CN201832656U (en) | White spirit waste diatomite regeneration device | |
| CN208218528U (en) | A kind of dirty, domestic sewage treatment device for shunting only | |
| CN206901985U (en) | A kind of sewage-treatment plant | |
| CN210528660U (en) | Low-cost iron and manganese removal water purification unit | |
| CN210885398U (en) | Protein separator | |
| CN109081516A (en) | A kind of river wastewater processing unit | |
| CN219239361U (en) | Slag overflow fine sand recovery device | |
| CN204151195U (en) | Integral type sewage biological denitrificaion treatment unit | |
| CN212799954U (en) | Novel improvement dissolved air flotation device | |
| CN216445158U (en) | Buffering catalytic oxidation equipment for sewage treatment | |
| CN205527807U (en) | Air boosting formula water purification installation that H type was arranged | |
| CN218478609U (en) | Integrated waste water reusing device for bathing place |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |