CN209039125U - A kind of iron-carbon micro-electrolysis tower processing system - Google Patents
A kind of iron-carbon micro-electrolysis tower processing system Download PDFInfo
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- CN209039125U CN209039125U CN201821480985.2U CN201821480985U CN209039125U CN 209039125 U CN209039125 U CN 209039125U CN 201821480985 U CN201821480985 U CN 201821480985U CN 209039125 U CN209039125 U CN 209039125U
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- electrolysis tower
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Abstract
The utility model discloses a kind of iron-carbon micro-electrolysis tower processing systems.Including iron-carbon micro-electrolysis tower, the middle part of iron-carbon micro-electrolysis tower is equipped with multilayer and flase floor is isolated, and is isolated on flase floor and is equipped with iron carbon body particle, and the lower section that flase floor is isolated in lowest level is equipped with porous water distributing plate, and the lower section of porous water distributing plate is sludge collecting tank；Gas distribution pipe is equipped in the sludge collecting tank, the nozzle that gas distribution pipe stretches out iron-carbon micro-electrolysis tower is pressure-air import；The sludge collecting tank is connected to sewage pipe, and sewage pipe is equipped with D valve.Tthe utility model system has iron carbon body particle in iron-carbon micro-electrolysis tower not easy to harden, and mass-transfer efficiency is high；Can meet an urgent need production in the event of a failure；Into conditioning tank sewage exception when will not influence the normal operation of system the advantages of, while also having many advantages, such as that structure is simple, complete function, capacity of resisting impact load are strong, stable and reliable operation.
Description
Technical field
The utility model relates to a kind of iron-carbon micro-electrolysis tower processing structure, especially a kind of iron-carbon micro-electrolysis tower processing system
System.
Background technique
Now at present for processed containing a small amount of heavy metal ion by traditional chemical routes from pretreatment system
Electroplating sewerage, it will usually use iron-carbon micro-electrolysis tower, but traditional iron-carbon micro-electrolysis tower can be deposited in use for some time
In the iron carbon body particle problem low with mass-transfer efficiency easy to harden；And in iron-carbon micro-electrolysis tower maintenance or failure, entire iron carbon is micro-
Tower processing system is electrolysed without emergency means, needs to stop production to debug；When traditional light electrolysis tower water intake mode " under into upper
It, can synthesis to conditioning tank and backward out " from when taking the suspended matter generated in a large amount of light electrolysis tower operational process in overflow pipe out of
Processing each process brings great impact load, or even seriously affects system discharge outlet water quality, at this moment can seriously affect system
It operates normally.
In summary: the prior art has iron carbon body particle easy to harden low with mass-transfer efficiency, in iron-carbon micro-electrolysis tower failure
When need stop production to debug, into conditioning tank sewage exception when will affect system normal operation defect.
Summary of the invention
The purpose of the utility model is to provide a kind of iron-carbon micro-electrolysis tower processing systems.It is with iron-carbon micro-electrolysis tower
Middle iron carbon body particle is not easy to harden, and mass-transfer efficiency is high；Can meet an urgent need production in the event of a failure；Into conditioning tank sewage exception when
The advantages of will not influence the normal operation of system.
The technical solution of the utility model includes: a kind of iron-carbon micro-electrolysis tower processing system, including iron-carbon micro-electrolysis tower, iron carbon are micro-
The middle part for being electrolysed tower is equipped with multilayer and flase floor is isolated, and is isolated on flase floor and is equipped with iron carbon body particle, flase floor is isolated in lowest level
Lower section be equipped with porous water distributing plate, the lower section of porous water distributing plate is sludge collecting tank；Gas distribution pipe is equipped in the sludge collecting tank,
The nozzle that gas distribution pipe stretches out iron-carbon micro-electrolysis tower is pressure-air import；The sludge collecting tank is connected to sewage pipe, sewage pipe
It is equipped with D valve.
In iron-carbon micro-electrolysis tower processing system above-mentioned, the gas distribution pipe is equipped with multiple air outlets in sludge collecting tank.
In iron-carbon micro-electrolysis tower processing system above-mentioned, the top of the iron-carbon micro-electrolysis tower is connected by overflow pipe to be adjusted
Pond；The sewage pipe connects sludge-tank；The gas distribution pipe for stretching out iron-carbon micro-electrolysis tower is equipped with B valve；The iron-carbon micro-electrolysis
The lower part of tower connects sewage water inlet pipe, and the nozzle of sewage water inlet pipe is pretreating sewage import, and sewage water inlet pipe is equipped with A valve,
Branch pipe is connected on sewage water inlet pipe between pretreating sewage import and A valve, branch pipe connects conditioning tank, and branch pipe is equipped with C valve.
In iron-carbon micro-electrolysis tower processing system above-mentioned, drinking-water pipe is equipped in the conditioning tank, drinking-water pipe connection is coaxial certainly
Suction centrifugal pump, coaxial self priming centrifugal pump connect outlet pipe, and outlet pipe is equipped with E valve, and the nozzle of outlet pipe is to go to General Office
Process interface after reason, one end of connection reflux branch pipe on the outlet pipe between E valve and coaxial self priming centrifugal pump, flow back branch pipe
The other end connects sludge-tank, and reflux branch pipe is equipped with F valve.
The utility model has the beneficial effects that compared with prior art, present treatment system is mainly by iron-carbon micro-electrolysis tower, adjusting
Pond, sludge-tank three parts are constituted, processed containing a small amount of weight by traditional chemical routes from pretreatment system for handling
The electroplating sewerage of metal ion, has the advantages that
1, the structure of the iron-carbon micro-electrolysis tower of the utility model mainly includes porous water distributing plate, gas distribution pipe, isolation grid, dirt
The isolation grid of mud collecting tank and blowdown valve etc., multilayer setting separates iron carbon body particle, which efficiently solves conventional iron
The problems such as iron carbon body particle is easy to harden existing for carbon micro-electrolysis tower, mass-transfer efficiency is low；
2, the utility model opens A valve, B valve under accidental conditions, closes C valve, at this moment passes through the micro- electricity of iron carbon
Solving tower, treated that sewage enters in conditioning tank, and sludge and suspended matter enter in sludge-tank；When light electrolysis tower needs to change iron carbon body
Particle or maintenance and when cisco unity malfunction, the pipeline and valve being connected to by converting conditioning tank with light electrolysis tower, future
It is introduced directly into conditioning tank from the electroplating sewerage of pretreatment system, only the appropriate adjustment technological parameter in preprocessing system, Ji Kebao
Hinder sewage treatment total system to operate normally, to effectively avoid stopping production caused by because of light electrolysis tower maintenance or failure, greatly mention
High the stable operation ability of sewage disposal system, operation at this time close A valve, open B valve, C valve, finely tune pretreatment system
Technological parameter can meet interim emergency production without stopping production；
3, the utility model under normal production scenarios, open by E valve, and F valve is closed, and conditioning tank is micro- from iron carbon for collecting
It is electrolysed the sewage of tower, and pumps and is handled toward subsequent handling；When the sewage from iron-carbon micro-electrolysis tower occurs abnormal, E valve is closed, F
Valve is opened, and abnormal sewage is transferred in sludge-tank, has won grace time and (one in the short time for Check System abnormal cause
As or so half a day, the specific time must be depending on carrying out water) do not influence system normal operation.
In summary: Tthe utility model system has iron carbon body particle in iron-carbon micro-electrolysis tower not easy to harden, mass-transfer efficiency
It is high；Can meet an urgent need production in the event of a failure；Into conditioning tank sewage exception when will not influence the normal operation of system the advantages of,
Also have many advantages, such as that structure is simple, complete function, capacity of resisting impact load are strong, stable and reliable operation simultaneously.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the attachment structure schematic diagram of iron-carbon micro-electrolysis tower；
Fig. 3 is the partial approach schematic diagram of a-quadrant in Fig. 1.
The label in accompanying drawing is: 1- iron-carbon micro-electrolysis tower, 2- isolation flase floor, 3- iron carbon body particle, the porous water distributing plate of 4-,
5- sludge collecting tank, 6- gas distribution pipe, 7- pressure-air import, 8- sewage pipe, 9-D valve, 10- air outlet, 11- overflow pipe, 12- tune
Section pond, 13- sludge-tank, 14- sewage water inlet pipe, 15- pretreating sewage import, 16-A valve, 17- branch pipe, 18-B valve, 19-C valve,
20- drinking-water pipe, the coaxial self priming centrifugal pump of 21-, 22- outlet pipe, 23-E valve, 24- remove process interface after integrated treatment, and 25- is returned
Flow branch pipe, 26-F valve.
Specific embodiment
The utility model is further described with reference to the accompanying drawings and examples, but is not intended as to the utility model
The foundation of limitation.
Embodiment.A kind of iron-carbon micro-electrolysis tower processing system constitutes such as Fig. 1-3, and shown includes iron-carbon micro-electrolysis tower 1, iron
The middle part of carbon micro-electrolysis tower 1 is equipped with multilayer and flase floor 2 is isolated, and is isolated on flase floor 2 and is equipped with iron carbon body particle 3, lowest level every
The lower section of screen 2 out of place is equipped with porous water distributing plate 4, and the lower section of porous water distributing plate 4 is sludge collecting tank 5；The sludge collecting tank 5
In be equipped with gas distribution pipe 6, gas distribution pipe 6 stretch out iron-carbon micro-electrolysis tower 1 nozzle be pressure-air import 7；The sludge collecting tank 5 with
Sewage pipe 8 is connected to, and sewage pipe 8 is equipped with D valve 9.
The isolation iron carbon body of flase floor 2 is isolated by the way that multilayer is arranged in iron-carbon micro-electrolysis tower 1 with anti-compaction in the utility model；
It is uniform to guarantee that the electroplating sewerage for entering iron-carbon micro-electrolysis tower 1 shunts for 6 structure novel of porous water distributing plate 4 and gas distribution pipe；Treated
The suspended matter generated during sludge and cleaning iron carbon body is located in the sludge collecting tank 5 of 1 bottom of iron-carbon micro-electrolysis tower, passes through row
Dirty pipe 8 can be discharged, and D valve 9 is the control valve of sewage pipe 8.
The gas distribution pipe 6 is equipped with multiple air outlets 10 in sludge collecting tank 5.
Multiple air outlets 10 can make the gas entered from pressure-air import 7 preferably disturb electroplating sewerage.
The top of the iron-carbon micro-electrolysis tower 1 connects conditioning tank 12 by overflow pipe 11；The sewage pipe 8 connects sludge-tank
13；The gas distribution pipe 6 for stretching out iron-carbon micro-electrolysis tower 1 is equipped with B valve 18；The lower part of the iron-carbon micro-electrolysis tower 1 connects sewage
Water inlet pipe 14, the nozzle of sewage water inlet pipe 14 are pretreating sewage import 15, and sewage water inlet pipe 14 is equipped with A valve 16, pretreatment
It is connected with branch pipe 17 on sewage water inlet pipe 14 between wastewater inlet 15 and A valve 16, branch pipe 17 connects conditioning tank 12, on branch pipe 17
Equipped with C valve 19.
The utility model need to only open A valve 16, B valve 18 under accidental conditions, close C valve 19, the course of work
Be: pretreating sewage enters from pretreating sewage import 15, then from carrying out in the entrance iron-carbon micro-electrolysis tower 1 of sewage water inlet pipe 14
Reason, while high pressure gas enters in iron-carbon micro-electrolysis tower 1 processing for accelerating sewage, processing from pressure-air import 7 from gas distribution pipe 6
Sewage afterwards enters in conditioning tank 12 from overflow pipe 11.
And when 1 failure of iron-carbon micro-electrolysis tower or when needing repairing, the case where total system can still run to meet production requirement,
At this moment only need to close A valve 16, B valve 18, open C valve 19, the course of work is: pretreating sewage from pretreating sewage into
Then mouth 15, which enters, not to be entered in iron-carbon micro-electrolysis tower 1, but pass through branch pipe 17 and enter in conditioning tank 12, is interim emergency production
Solution is provided without stopping production, only needs to finely tune pretreatment system technological parameter at this time.
Drinking-water pipe 20 is equipped in the conditioning tank 12, drinking-water pipe 20 connects coaxial self priming centrifugal pump 21, coaxial self-priming
Centrifugal pump 21 connects outlet pipe 22, and outlet pipe 22 is equipped with E valve 23, and the nozzle of outlet pipe 22 is to remove process interface after integrated treatment
One end of connection reflux branch pipe 25 on outlet pipe 22 between 24, E valves 23 and coaxial self priming centrifugal pump 21, reflux branch pipe 25
The other end connects sludge-tank 13, and reflux branch pipe 25 is equipped with F valve 26.
The utility model under normal production scenarios, open by E valve 23, and F valve 26 is closed, at this moment in coaxial self priming centrifugal pump
Under the action of 21, the sewage in conditioning tank 12 passes through coaxial self priming centrifugal pump 21 from drinking-water pipe 20, enters back into outlet pipe 22, then
Process interface 24 is discharged after going integrated treatment, i.e., by treated, sewage is sent into subsequent handling.
When the sewage from iron-carbon micro-electrolysis tower 1 occurs abnormal, E valve 23 is closed, and F valve 26 is opened, at this moment conditioning tank 12
In abnormal sewage can from from drinking-water pipe 20 pass through coaxial self priming centrifugal pump 21, enter back into reflux branch pipe 25, enter back into sludge
In pond 13, grace time has been won for Check System abnormal cause and (or so general half a day, the specific time, which must regard, comes in the short time
Depending on water) system normal operation is not influenced.
Claims (4)
1. a kind of iron-carbon micro-electrolysis tower processing system, it is characterised in that: including iron-carbon micro-electrolysis tower (1), iron-carbon micro-electrolysis tower (1)
Middle part be equipped with multilayer isolation flase floor (2), be equipped with iron carbon body particle (3) in isolation flase floor (2), grid is isolated in lowest level
The lower section of plate (2) is equipped with porous water distributing plate (4), and the lower section of porous water distributing plate (4) is sludge collecting tank (5)；The sludge is collected
Gas distribution pipe (6) are equipped in slot (5), the nozzle that gas distribution pipe (6) stretches out iron-carbon micro-electrolysis tower (1) is pressure-air import (7)；It is described
Sludge collecting tank (5) is connected to sewage pipe (8), and sewage pipe (8) is equipped with D valve (9).
2. iron-carbon micro-electrolysis tower processing system according to claim 1, it is characterised in that: the gas distribution pipe (6) is in sludge
Multiple air outlets (10) are equipped in collecting tank (5).
3. iron-carbon micro-electrolysis tower processing system according to claim 1, it is characterised in that: the iron-carbon micro-electrolysis tower (1)
Top by overflow pipe (11) connection conditioning tank (12)；The sewage pipe (8) connects sludge-tank (13)；The stretching iron carbon is micro-
The gas distribution pipe (6) for being electrolysed tower (1) is equipped with B valve (18)；The lower part of the iron-carbon micro-electrolysis tower (1) connects sewage water inlet pipe
(14), the nozzle of sewage water inlet pipe (14) is pretreating sewage import (15), and sewage water inlet pipe (14) is equipped with A valve (16), in advance
It is connected with branch pipe (17) on sewage water inlet pipe (14) between processing wastewater inlet (15) and A valve (16), branch pipe (17) connection is adjusted
It saves pond (12), branch pipe (17) is equipped with C valve (19).
4. iron-carbon micro-electrolysis tower processing system according to claim 3, it is characterised in that: be equipped in the conditioning tank (12)
Drinking-water pipe (20), drinking-water pipe (20) connect coaxial self priming centrifugal pump (21), and coaxial self priming centrifugal pump (21) connects outlet pipe
(22), outlet pipe (22) is equipped with E valve (23), and the nozzle of outlet pipe (22) is to remove process interface (24) after integrated treatment, E valve
(23) one end that reflux branch pipe (25) is connected on the outlet pipe (22) between coaxial self priming centrifugal pump (21), flow back branch pipe
(25) the other end connects sludge-tank (13), and reflux branch pipe (25) is equipped with F valve (26).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821480985.2U CN209039125U (en) | 2018-09-11 | 2018-09-11 | A kind of iron-carbon micro-electrolysis tower processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821480985.2U CN209039125U (en) | 2018-09-11 | 2018-09-11 | A kind of iron-carbon micro-electrolysis tower processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209039125U true CN209039125U (en) | 2019-06-28 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821480985.2U Active CN209039125U (en) | 2018-09-11 | 2018-09-11 | A kind of iron-carbon micro-electrolysis tower processing system |
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| Country | Link |
|---|---|
| CN (1) | CN209039125U (en) |
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2018
- 2018-09-11 CN CN201821480985.2U patent/CN209039125U/en active Active
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