CN207002335U - Constant pressure type sewage oxidizing treater - Google Patents
Constant pressure type sewage oxidizing treater Download PDFInfo
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- CN207002335U CN207002335U CN201720254901.2U CN201720254901U CN207002335U CN 207002335 U CN207002335 U CN 207002335U CN 201720254901 U CN201720254901 U CN 201720254901U CN 207002335 U CN207002335 U CN 207002335U
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- tank body
- electrode plate
- constant pressure
- pressure type
- type sewage
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Abstract
It the utility model is related to a kind of sewage disposal device,More particularly, to a kind of simple in construction,Operating cost is relatively low and sewage is formed flow-disturbing effect during electrochemical decomposition so as to prevent polarization,It is passivated and the high constant pressure type sewage oxidizing treater of operating efficiency,Including tank body one (1),Tank body two (2),Electrode plate groups (3) are multiple,The tank body one (1) connects with tank body two (2),The electrode plate groups (3) are located on the inwall of tank body one (1) and tank body two (2),Electrode plate groups (3) in the tank body one (1) and tank body two (2) are six and each two forms one group,Every group of electrode plate groups (3) is located in same perpendicular,Two adjacent groups electrode plate groups (3) intersect each other in perpendicular,Also include water inlet (4) and delivery port (5),The water inlet (4) is located on tank body one (1),The delivery port (5) is located on tank body two (2).
Description
Technical field
A kind of sewage disposal device is the utility model is related to, more particularly, to a kind of constant pressure type sewage oxidizing treater.
Background technology
At present, substantial amounts of heavy metal ion is contained in the sewage that industrial production is formed, it is coloured such as Electroplate Factory's plating piece washings
Metallurgical works dedusting draining etc..It is often more and the heavy metal contained in the waste water of actually required processing is not single kind
Heavy metal species are simultaneously deposited, and threat of these heavy metal ion to environment structure is very big.
When handling the waste water containing heavy metal, if the metal ion that positive plate discharges is not diffused into water body timely
In, pole plate easily occur polarization, passivation phenomenon, so as to cause the sewage disposal time grow, high energy consumption, active material be released into it is uneven,
The moisture content of dregs is higher and the problems such as continuity of operation is poor.
Utility model content
For above-mentioned deficiency of the prior art, the utility model offer one kind is simple in construction, operating cost is relatively low and makes
Sewage forms flow-disturbing effect so as to prevent polarization, passivation and the high constant pressure type of operating efficiency during electrochemical decomposition
Sewage oxidizing treater.
To realize above technical purpose, the technical solution of the utility model is:A kind of constant pressure type sewage oxidizing treater,
Including tank body one, tank body two, electrode plate groups are multiple, the tank body one connects with tank body two, and the electrode plate groups are located at tank body one
On the inwall of tank body two, the electrode plate groups in the tank body one and tank body two are six and each two forms one group, every group
Electrode plate groups are located in same perpendicular, and two adjacent groups electrode plate groups intersect each other in perpendicular, in addition to water inlet and
Delivery port, the water inlet are located on tank body one, and the delivery port is located on tank body two, and aeration tube is provided with the tank body two,
The aeration tube is provided with gum sleeve, and the gum sleeve is provided with venthole.
Preferably, the metallic plate group is at least four electrode plates.
Preferably, perpendicular degree of the being crossed to form angle that the two adjacent groups electrode plate groups are formed.
Preferably, the water inlet is located at the bottom of tank body one.
Preferably, the delivery port is located at the top of tank body two.
Preferably, the tank body one connects with tank body two refers to that the top of tank body one connects with the bottom of tank body two.
Preferably, the battery lead plate is composite construction, include metal substrate, low carbon steel plate and electrode successively from inside to outside
Plate.
Preferably, it is some to be equipped with cellular through hole on each battery lead plate.
Above description can be seen that the utility model and possess advantages below：Sewage is passed through tank to the utility model when in use
Because electrode plate groups are located on the inwall of tank body one and tank body two and every group of electrode plate groups are located in same perpendicular after body one,
The perpendicular that two adjacent groups electrode plate groups are formed intersects each other, and sewage can form the effect of eddy flow in tank body one and tank body two
Fruit, while the pressure of water inlet reaches a timing, the effect of eddy flow is stronger, can not only be improved using the design of double tank bodies
The efficiency of electrochemistry sewage disposal, while sewage is also extremely strong to the developing result of electrode plate groups, so as to ensure the effect used.
Brief description of the drawings
Fig. 1 is the sectional view of constant pressure type sewage oxidizing treater of the present utility model；
Fig. 2 is the top view of constant pressure type sewage oxidizing treater of the present utility model；
Fig. 3 is the side view of the aeration tube of constant pressure type sewage oxidizing treater of the present utility model.
Brief description of the drawings：1st, tank body one, 2, tank body two, 3, electrode plate groups, 4, water inlet, 5, delivery port, 6, aeration tube, 61,
Gum sleeve.
Embodiment
As illustrated, a kind of constant pressure type sewage oxidizing treater, including tank body 1, tank body 22, electrode plate groups more than 3
Individual, described tank body 1 is connected with tank body 22, and the electrode plate groups 3 are located on the inwall of tank body 1 and tank body 22, the tank
Electrode plate groups 3 in body 1 and tank body 22 are six and each two forms one group, and every group of electrode plate groups 3 are positioned at same vertical
In plane, two adjacent groups electrode plate groups 3 intersect each other in perpendicular, in addition to water inlet 4 and delivery port 5, the water inlet 4
It is located on tank body 1, the delivery port 5 is located on tank body 22；Aeration tube 6 is provided with the tank body 22, in the aeration tube 6
Provided with gum sleeve 61, the gum sleeve 61 is provided with venthole；The metallic plate group 3 is at least four electrode plates；It is described
The perpendicular that two adjacent groups electrode plate groups 3 are formed is crossed to form 45 degree of angles；The water inlet 4 is located at the bottom of tank body 1；Institute
State delivery port 5 and be located at the top of tank body 22；The tank body 1 connects the top and the bottom of tank body 22 for referring to tank body 1 with tank body 22
Portion connects；The battery lead plate is composite construction, includes metal substrate, low carbon steel plate and battery lead plate successively from inside to outside；Each electricity
It is some that cellular through hole is equipped with pole plate.
Sewage is passed through after tank body one because electrode plate groups are located in tank body one and tank body two the utility model when in use
On wall and every group of electrode plate groups are located in same perpendicular, and the perpendicular that two adjacent groups electrode plate groups are formed intersects each other,
Sewage can form the effect of eddy flow in tank body one and tank body two, while the pressure of water inlet reaches a timing, the effect of eddy flow
It is more strong, the efficiency of electrochemistry sewage disposal can not only be improved using the design of double tank bodies, while sewage is to electrode plate groups
Developing result it is also extremely strong, so as to ensure the effect used；Furthermore because battery lead plate is composite construction, include successively from inside to outside
Metal substrate, low carbon steel plate and battery lead plate, further electrolytic efficiency can be improved while flow velocity is very fast, so as to ensure to make
The electrolysis effectiveness of used time；Whole constant pressure type sewage oxidizing treater is intake using malleation, negative pressure water outlet, not only may be used in a device
To realize that electrolytic sewage can also carry out back flush；Electrode can effectively be prevented by carrying out aeration to sewage using aeration tube simultaneously
Plate is passivated, and being arranged with gum sleeve on aeration tube effectively can prevent aeration tube from silting occur.
The utility model and embodiments thereof are described above, this describe it is no restricted, shown in accompanying drawing
Also it is one of embodiment of the present utility model, actual structure is not limited thereto.All in all if this area it is general
Logical technical staff is enlightened by it, in the case where not departing from the utility model and creating objective, without designing with being somebody's turn to do for creativeness
The similar frame mode of technical scheme and embodiment, all should belong to the scope of protection of the utility model.
Claims (8)
1. a kind of constant pressure type sewage oxidizing treater, including tank body one (1), tank body two (2), electrode plate groups (3) are multiple, described
Tank body one (1) is connected with tank body two (2), and the electrode plate groups (3) are located on the inwall of tank body one (1) and tank body two (2), described
Electrode plate groups (3) in tank body one (1) and tank body two (2) are six and each two forms one group, every group of electrode plate groups (3) position
In in same perpendicular, two adjacent groups electrode plate groups (3) intersect each other in perpendicular, in addition to water inlet (4) and water outlet
Mouth (5), the water inlet (4) are located on tank body one (1), and the delivery port (5) is located on tank body two (2), the tank body two (2)
In be provided with aeration tube (6), the aeration tube (6) is provided with gum sleeve (61), and the gum sleeve (61) is provided with venthole.
2. constant pressure type sewage oxidizing treater according to claim 1, it is characterised in that：The electrode plate groups (3) are
At least four electrode plates.
3. constant pressure type sewage oxidizing treater according to claim 1, it is characterised in that：The two adjacent groups battery lead plate
The perpendicular that group (3) is formed is crossed to form 45 degree of angles.
4. constant pressure type sewage oxidizing treater according to claim 1, it is characterised in that：The water inlet (4) is located at
Tank body one (1) bottom.
5. constant pressure type sewage oxidizing treater according to claim 1, it is characterised in that：The delivery port (5) is located at
Tank body two (2) top.
6. constant pressure type sewage oxidizing treater according to claim 1, it is characterised in that：The tank body one (1) and tank
Body two (2) connection refers to that the top of tank body one (1) connects with tank body two (2) bottom.
7. constant pressure type sewage oxidizing treater according to claim 2, it is characterised in that：It is characterized in that：The electricity
Pole plate is composite construction, includes metal substrate, low carbon steel plate and battery lead plate successively from inside to outside.
8. constant pressure type sewage oxidizing treater according to claim 2, it is characterised in that：It is equipped with each battery lead plate
Cellular through hole is some.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720254901.2U CN207002335U (en) | 2017-03-16 | 2017-03-16 | Constant pressure type sewage oxidizing treater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720254901.2U CN207002335U (en) | 2017-03-16 | 2017-03-16 | Constant pressure type sewage oxidizing treater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207002335U true CN207002335U (en) | 2018-02-13 |
Family
ID=61428496
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720254901.2U Active CN207002335U (en) | 2017-03-16 | 2017-03-16 | Constant pressure type sewage oxidizing treater |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207002335U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106809923A (en) * | 2017-03-16 | 2017-06-09 | 宜兴市坤佳环境科技有限公司 | Constant pressure type sewage oxidizing treater |
-
2017
- 2017-03-16 CN CN201720254901.2U patent/CN207002335U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106809923A (en) * | 2017-03-16 | 2017-06-09 | 宜兴市坤佳环境科技有限公司 | Constant pressure type sewage oxidizing treater |
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