CN205973916U - Little electrolytic reaction tower of iron carbon - Google Patents
Little electrolytic reaction tower of iron carbon Download PDFInfo
- Publication number
- CN205973916U CN205973916U CN201620864489.1U CN201620864489U CN205973916U CN 205973916 U CN205973916 U CN 205973916U CN 201620864489 U CN201620864489 U CN 201620864489U CN 205973916 U CN205973916 U CN 205973916U
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- tower body
- iron
- reaction tower
- carbon micro
- electrolysis reaction
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Abstract
The utility model discloses a little electrolytic reaction tower of iron carbon, including the tower body, tower body upper portion is equipped with water inlet, delivery port and air inlet, the water inlet is located the downside of delivery port, the tower body bottom is equipped with and has row bagger of mud mouth, the tower body lower part is located the top of bagger, is equipped with aerator, filter plate and water distribution device from bottom to top in proper order, the aerator links to each other with the air inlet. The utility model discloses simple structure reacts indisputable carbon filler and is difficult for hardening, arranges the sediment thoroughly, totally, and unblocked in the reaction tower, it is on -the -spot inner wall cutout and bias flow can not to appear, and the observation of being convenient for is overhauld, and the treatment effeciency is high, and the treatment effect is good.
Description
Technical field
This utility model belongs to field of water treatment equipment, especially relates to a kind of iron-carbon micro-electrolysis reaction tower.
Background technology
It is increasingly difficult to degrade with wastewater from chemical industry, dyeing waste water etc., iron-carbon micro-electrolysis receive much concern as preprocess method.
Iron-carbon micro-electrolysis are to utilize Principles of Metal Erosion, form the technique that galvanic element is processed to high concentrated organic wastewater, and it is with useless
Paper gives up, and operating cost is low, and it can cut down the COD in waste water significantly, and can improve the biodegradability of used water difficult to degradate, in China's tool
There is good prospects for commercial application.But it is easily hardened to there is filler in existing iron-carbon micro-electrolysis system during using,
Equipment inner wall cutout or bias current, iron cement relatively more is difficult discharge etc..
Utility model content
In order to overcome the deficiencies in the prior art, this utility model provide a kind of water outlet uniformly, filler be difficult knot tying, at waste water
The good iron-carbon micro-electrolysis reaction tower of reason effect.
This utility model solves its technical problem and be employed technical scheme comprise that：A kind of iron-carbon micro-electrolysis reaction tower, including
Tower body, described tower body top is provided with water inlet, outlet and air inlet, and described water inlet is located at the downside of outlet；Described tower
Body bottom is provided with the bucket with mud discharging mouth, described tower body bottom be located at bucket top, be sequentially provided with from bottom to top aerator,
Filter plate and water-distributing device, described aerator is connected with air inlet.The lower section being located at water inlet in the bottom of tower body is provided with water distribution
, so that water inlet be fully contacted can uniformly and with ferrum carbon filler, reaction is more efficient for device；It is provided with aerator below filter plate, make
The particles such as iron cement are in suspended state, it is to avoid be attached to the surface of ferrum carbon filler so that filler be difficult hardened；Open on filter plate
It is provided with uniform hole it is ensured that gas and backwash water are evenly distributed.
Further, the tapered structure of described bucket, mud discharging mouth is located at the bottom cone mouth of bucket.Iron-carbon micro-electrolysis reacted
The body refuse producing in journey is deposited in bucket by filter plate, is carried out it is not necessary to take out ferrum carbon filler by mud discharging mouth regular discharge
Deslagging, conical design also makes bucket bottom spoil disposal more thorough.
Further, the top of described water inlet is provided with gap.
Further, described tower body is provided with the visual window of observable tower body inner case.It is easy to aeration in facilities for observation
Whether good, amount of float etc., it is easy to operator and judge whether to need discharging to overhaul.
Further, described tower body is provided with discharge port.Be not only convenient for overhaul, and can discharging at discharge port, subtract
The labor intensity of little discharging.
Further, described aerator is provided with the through hole being obliquely installed.
Further, described through hole is from the downward-sloping 45 ° of settings of aerator central shaft.Aerator is given vent to anger more equal
Even, and it is prevented effectively from blocking through hole.
Further, on described tower body, the position corresponding with outlet is provided with effluent weir.Waste water is from top water outlet, top
Effluent weir make water outlet more uniform, water-distributing device and effluent weir cooperation can avoid that inwall cutout in waste water and bias current is existing
As.
Further, described air inlet can be connected as backwash water inlet with back purge system.Air inlet and backwash dress
Putting into water is same openning, it is to avoid pipeline complicates, and prevents aerator from blocking, the major function of back purge system is to prevent mud
Slag deposits, in ferrum carbon filler surface, fully can clean ferrum carbon filler surface and equipment inner wall it is ensured that flowing in equipment with air water with entering
Road is unimpeded.
The beneficial effects of the utility model are：Structure is simple, reaction ferrum carbon filler be difficult hardened, deslagging thoroughly, clean, instead
Answer unimpeded in tower, be not in inwall cutout and bias current scene, be easy to observe maintenance, treatment effeciency is high, high treating effect.
Brief description
Fig. 1 is structural representation one of the present utility model.
Fig. 2 is structural representation two of the present utility model.
Fig. 3 is overlooking the structure diagram of the present utility model.
Fig. 4 is A-A cross-sectional view of the present utility model.
Fig. 5 is the part-structure schematic diagram of aerator.
Fig. 6 is the cross-sectional view of aerator.
Specific embodiment
In order that those skilled in the art are better understood from this utility model scheme, real below in conjunction with this utility model
Apply the accompanying drawing in example, the technical scheme in this utility model embodiment is carried out with clear, complete description it is clear that described
Embodiment is only a part of embodiment of the present utility model, rather than whole embodiments.Based on the reality in this utility model
Apply example, the every other embodiment that those of ordinary skill in the art are obtained under the premise of not making creative work, all answer
When the scope belonging to this utility model protection.
Shown in reference picture 1-6, a kind of iron-carbon micro-electrolysis reaction tower, including the tower body 1 in hollow cylindrical, the top of tower body 1
It is provided with water inlet 11, outlet 12 and gap 14, water inlet 11 place horizontal plane is located at outlet 12 place horizontal plane slightly
Lower position, corresponding tower body 1 at outlet 12 is provided with effluent weir 17, and gap 14 is located at the upper position of water inlet 11
Put, and gap 14 place horizontal plane is located at the upper side position of outlet 12 place horizontal plane.The bottom of tower body 1 is provided with bucket
2, the tapered structure of bucket 2, mud discharging mouth 21 is located at the cone mouth of bucket 2 bottom.Carry out ferrum carbon micro- in iron-carbon micro-electrolysis reaction tower
The body refuse producing during cell reaction is deposited in bucket 2 by filter plate 4, is outwards discharged by mud discharging mouth 21 timing, is not required to
Take out filler deslagging, deslagging is more thorough.
The bottom of tower body 1, positioned at the top of bucket 2, is sequentially installed with aerator 3, filter plate 4 and water-distributing device from bottom to top
5.Aerator 3 is connected with the air inlet 13 being opened in tower body 1 bottom.Through hole 31, through hole is uniformly offered on the side wall of aerator 3
31 tilt 45 ° of settings from vertical direction to side, not only give vent to anger uniformly, and are prevented effectively from it and are blocked.Uniformly open on filter plate 4
It is provided with hole it is ensured that the distribution of gas and backwash water is more uniform.Air inlet 13 can be connected with back purge system, will air inlet
Mouth 13 uses as backwash water inlet, simplifies pipeline, back purge system can prevent subsidence settling on the surface of filler, works as gas
Body and water enter from air inlet 13 simultaneously, can fully clean the inwall on filler surface and tower body 1 it is ensured that tower body 1 inner flow passage is smooth
Logical, it is to avoid aerator 3 blocks.
The visual window 15 being made up of transparent material and discharge port 16 are provided with the side wall of tower body 1, discharge port 16 is located at tower
The bottom of body 1.Operator can observe the internal situation of tower body 1 by visual window 15, the amassing of such as aeration situation, float
Tired amount etc., is easy to the situation that operator arrive according to the observation and judges whether to need discharging to overhaul.When judging to need discharging, can beat
Material mouth of starting discharging 16 easily discharging, substantially reduces the labor intensity of discharging, is also convenient in maintenance.
Operation principle of the present utility model is：When equipment normally runs, waste water enters in tower body 1 from water inlet 11, leads to
Cross water-distributing device 5 to be uniformly laid in iron-carbon micro-electrolysis reaction tower, the ferrum carbon filler effect with tower body 1 bottom, air is from air inlet
Mouth 13 passes through aerator 3 and enters in tower body 1 from bottom, is evenly distributed in the water body in tower body 1, passes through through the waste water of reaction
Effluent weir 17 overflows, and flows out tower body 1 from outlet 12.
When observing that tower body 1 bottom float is more by visual window 15, when needing to carry out spoil disposal and aeration backwash, close
Water inlet 11 and outlet 12, open mud discharging mouth 21 and carry out spoil disposal, after spoil disposal last for several minutes, close mud discharging mouth 21, open into
QI KOU 13 and back purge system, now air inlet 13 use as backwash water inlet, carry out aeration backwash, backwash water is from gap
14 discharge, after aeration backwash stand 15-30min, be again turned on mud discharging mouth 21 discharge 3-5min, after the completion of iron-carbon micro-electrolysis reaction
Tower puts into normal operating condition.
When iron-carbon micro-electrolysis reaction tower needs maintenance, close water inlet 11, outlet 12 and air inlet 13, open spoil disposal
Mouth 21, by the body refuse in tower body 1 and waste water emptying, is opened discharge port 16 and is carried out discharging inspection operation.
Above-mentioned specific embodiment is used for illustrating this utility model, rather than this utility model is limited,
In spirit of the present utility model and scope of the claims, any modifications and changes that this utility model is made, all fall
Enter protection domain of the present utility model.
Claims (9)
1. a kind of iron-carbon micro-electrolysis reaction tower, including tower body（1）, described tower body（1）Top is provided with water inlet（11）, outlet
（12）And air inlet（13）It is characterised in that：Described water inlet（11）Positioned at outlet（12）Downside；Described tower body（1）Bottom
Portion is provided with mud discharging mouth（21）Bucket（2）, described tower body（1）Bottom is located at bucket（2）Top, set successively from bottom to top
There is aerator（3）, filter plate（4）And water-distributing device（5）, described aerator（3）With air inlet（13）It is connected.
2. iron-carbon micro-electrolysis reaction tower according to claim 1 it is characterised in that：Described bucket（2）Tapered structure, row
Mud mouth（21）Positioned at bucket（2）Bottom cone mouth.
3. iron-carbon micro-electrolysis reaction tower according to claim 1 it is characterised in that：Described water inlet（11）Top be provided with
Gap（14）.
4. iron-carbon micro-electrolysis reaction tower according to claim 1 it is characterised in that：Described tower body（1）It is provided with observable
Tower body（1）The visual window of inner case（15）.
5. iron-carbon micro-electrolysis reaction tower according to claim 1 it is characterised in that：Described tower body（1）It is provided with discharge port
（16）.
6. iron-carbon micro-electrolysis reaction tower according to claim 1 it is characterised in that：Described aerator（3）It is provided with inclination
The through hole of setting（31）.
7. iron-carbon micro-electrolysis reaction tower according to claim 6 it is characterised in that：Described through hole（31）From aerator（3）
The downward-sloping 45 ° of settings of central shaft.
8. iron-carbon micro-electrolysis reaction tower according to claim 1 it is characterised in that：Described tower body（1）Go up and outlet
（12）Corresponding position is provided with effluent weir（17）.
9. iron-carbon micro-electrolysis reaction tower according to claim 1 it is characterised in that：Described air inlet（13）Can be with backwash
Device is connected as backwash water inlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620864489.1U CN205973916U (en) | 2016-08-10 | 2016-08-10 | Little electrolytic reaction tower of iron carbon |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620864489.1U CN205973916U (en) | 2016-08-10 | 2016-08-10 | Little electrolytic reaction tower of iron carbon |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205973916U true CN205973916U (en) | 2017-02-22 |
Family
ID=59978042
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620864489.1U Active CN205973916U (en) | 2016-08-10 | 2016-08-10 | Little electrolytic reaction tower of iron carbon |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205973916U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108658323A (en) * | 2018-06-25 | 2018-10-16 | 江苏宜裕环保科技有限公司 | A kind of intensifying method of high-concentration organic chemical wastewater pretreating process |
-
2016
- 2016-08-10 CN CN201620864489.1U patent/CN205973916U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108658323A (en) * | 2018-06-25 | 2018-10-16 | 江苏宜裕环保科技有限公司 | A kind of intensifying method of high-concentration organic chemical wastewater pretreating process |
| CN108658323B (en) * | 2018-06-25 | 2021-11-09 | 江苏宜裕环保科技有限公司 | Strengthening method of high-concentration organic chemical wastewater pretreatment process |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |