CN209651928U - A kind of floating degreasing unit of vapour - Google Patents
A kind of floating degreasing unit of vapour Download PDFInfo
- Publication number
- CN209651928U CN209651928U CN201822022781.0U CN201822022781U CN209651928U CN 209651928 U CN209651928 U CN 209651928U CN 201822022781 U CN201822022781 U CN 201822022781U CN 209651928 U CN209651928 U CN 209651928U
- Authority
- CN
- China
- Prior art keywords
- degreasing tank
- degreasing
- pressure air
- solution
- air tube
- 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.)
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- 238000005238 degreasing Methods 0.000 title claims abstract description 77
- 238000003760 magnetic stirring Methods 0.000 claims abstract description 14
- 239000000203 mixture Substances 0.000 claims abstract description 10
- 238000000926 separation method Methods 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- GVPFVAHMJGGAJG-UHFFFAOYSA-L cobalt dichloride Chemical compound [Cl-].[Cl-].[Co+2] GVPFVAHMJGGAJG-UHFFFAOYSA-L 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 229910052799 carbon Inorganic materials 0.000 description 2
- 229910017052 cobalt Inorganic materials 0.000 description 2
- 239000010941 cobalt Substances 0.000 description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000013019 agitation Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005137 deposition process Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
Landscapes
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Abstract
The utility model discloses a kind of vapour to float degreasing unit, including degreasing tank, magnetic stirring apparatus and multiple high-pressure air tubes, magnetic stirring apparatus is arranged in degreasing tank, and multiple high-pressure air tubes are uniformly plugged on the side wall of degreasing tank to float for being passed through air driven oil content to degreasing tank high pressure；The top of degreasing tank is provided with solution inlet port before oil removing, and lower part is provided with solution discharge tube after oil removing, and top is provided with the outlet of oil gas aqueous mixtures；The utility model pours air high speed in solution by multiple high-pressure air tubes, due to solution in degreasing tank high speed rotation, contact the solution in degreasing tank sufficiently, uniformly with air, after air is contacted with solution, form micro-bubble, oil content in solution rises to solution upper surface with bubble, and collect in oil content on medium swirl, oil gas aqueous mixtures outlet discharge can be directly provided at the top of degreasing tank using negative tube, structure is simple, production efficiency can be can be improved convenient for the separation of oil content in solution.
Description
Technical field
The utility model belongs to cobalt chloride degreasing unit technical field, and in particular to a kind of floating degreasing unit of vapour.
Background technique
The mode that extraction process and dissolution chlorinating dissolution cobalt chloride crystal are generallyd use in electrodeposited cobalt technique prepares cobalt chloride
Solution, and a small amount of solid particle polluter and oil content are all contained using the cobalt chloride solution that above two mode produces.
The content of oil content is generally between 20~50 mg/litres, and technique requires oil in 10 mg/litres hereinafter, otherwise
Cobalt plate meeting " layering of flaking " or " long blackening " etc. in electrolytic deposition process, common deoiling method are to use active carbon adsorption, but live
The property attached capacity of carbon is limited, and adsorbs in water solution system, and adsorbance is worse, per kilogram activity can only 10~20 oil contents, phase
When the cobalt chloride solution that can only handle 0.5~1 method in per kilogram activated carbon.In addition activated carbon impurity content is high, uses every time
It is preceding to use 10~20 times of pure water that manage again cleaning impurity that could use, trouble when use.
Utility model content
For overcome the deficiencies in the prior art, the purpose of the utility model is to provide a kind of vapour to float degreasing unit.
The utility model embodiment provides a kind of floating degreasing unit of vapour, including degreasing tank, magnetic stirring apparatus and multiple high pressures
Air hose, the magnetic stirring apparatus are arranged in degreasing tank, and the multiple high-pressure air tube is uniformly plugged in the side wall of degreasing tank
On for degreasing tank high pressure be passed through air driven oil content float；The top of the degreasing tank is provided with solution inlet port before oil removing,
The lower part of the degreasing tank is provided with solution discharge tube after oil removing, and oil gas aqueous mixtures are provided at the top of the degreasing tank and are gone out
Mouthful.
In above scheme, the multiple high-pressure air tube is divided into multiple high-pressure air tube groups, the multiple high-pressure air tube
Group from the bottom of degreasing tank to degreasing tank at the top of be arranged successively.
In above scheme, the multiple high-pressure air tube group is spaced substantially equidistant.
In above scheme, each high-pressure air tube group includes at least one high-pressure air tube, the high-pressure air tube
It is inserted into degreasing tank in the horizontal direction.
In above scheme, each high-pressure air tube group includes two high-pressure air tubes, described two high-pressure air tubes
Symmetrically it is plugged in the two sides of degreasing tank.
In above scheme, each high-pressure air tube is uniformly arranged multiple air outlets along axial direction.
In above scheme, the diameter of the air outlet is 3~5mm.
In above scheme, the oil gas aqueous mixtures outlet is connect with negative tube.
In above scheme, the magnetic stirring apparatus includes agitating paddle and magnetic driver, and degreasing tank is arranged in the agitating paddle
Bottom that is interior and being located at degreasing tank, the magnetic driver are arranged in the lower section of degreasing tank and connect with agitating paddle.
Compared with prior art, the utility model in degreasing tank by being arranged magnetic stirring apparatus and multiple pressure-airs
Pipe, magnetic stirring apparatus is able to drive the solution high speed rotation in degreasing tank, while air passes through multiple high-pressure air tube high-speed punchings
Enter in solution, due to solution in degreasing tank high speed rotation, and high-pressure air tube is to be evenly arranged in slot, is made in degreasing tank
Solution and air sufficiently, uniformly contact, after air is contacted with solution, formation micro-bubble, the oil content in solution is with bubble
Solution upper surface is risen to, and whirlpool can be formed on surface when due to solution rotating, so that oil content is collected on medium swirl, adopt
Oil gas aqueous mixtures outlet discharge can be directly provided at the top of degreasing tank with negative tube, the utility model structure is simple,
Production efficiency can be can be improved convenient for the separation of oil content in solution.
Detailed description of the invention
Fig. 1 is the main view that a kind of vapour provided by the embodiment of the utility model floats degreasing unit.
Appended drawing reference is as follows:
1 --- --- solution inlet port, 12 before oil removing --- solution discharge tube, 13 after oil removing --- oil gas water of degreasing tank, 11
Mixture outlet, 2 --- magnetic stirring apparatus, 21 --- agitating paddle, 22 --- magnetic driver, 3 --- high-pressure air tube,
31 --- air outlet.
Specific embodiment
In order to make the purpose of the utility model, technical solutions and advantages more clearly understood, with reference to embodiments with it is attached
Figure, the present invention will be further described in detail.It should be appreciated that specific embodiment described herein is only used to explain
The utility model is not used to limit the utility model.
The utility model embodiment provides a kind of floating degreasing unit of vapour, with reference to Fig. 1, including degreasing tank 1, magnetic stirring apparatus 2
With multiple high-pressure air tubes 3, the magnetic stirring apparatus 2 is arranged in degreasing tank 1, and the multiple high-pressure air tube 3 uniformly plugs
It floats on the side wall of degreasing tank 1 for being passed through air driven oil content to 1 high pressure of degreasing tank；The top of the degreasing tank 1 is arranged
There is solution inlet port 11 before oil removing, the lower part of the degreasing tank 1 is provided with solution discharge tube 12 after oil removing, the top of the degreasing tank 1
Portion is provided with oil gas aqueous mixtures outlet 13.
Magnetic stirring apparatus 2 includes agitating paddle 21 and magnetic driver 22, and the agitating paddle 21 is arranged in degreasing tank 1 and position
In the bottom of degreasing tank 1, the magnetic driver 22 is arranged in the lower section of degreasing tank 1 and connect with agitating paddle 21.
Agitating paddle 21, by magnetic drive, is not directly contacted with power transmission members in bottom, prevents driving member from polluting
In addition solution is magnetic drive, there is no the sealing of driving member, can be avoided the risk from bottom leakage.
Multiple high-pressure air tubes 3 divide for multiple high-pressure air tube groups, multiple high-pressure air tube groups from the bottom of degreasing tank 1 to
The top of degreasing tank 1 is arranged successively.
Multiple high-pressure air tube groups are spaced substantially equidistant, and pressure-air can be made uniformly to contact with solution.
Each high-pressure air tube group includes at least one high-pressure air tube 3, and high-pressure air tube 3 is inserted into oil removing in the horizontal direction
Slot 1.
General each high-pressure air tube group includes two high-pressure air tubes 3, and two high-pressure air tubes 3 are along the two of degreasing tank 1
Side symmetrically plugs, and for 3 one end of high-pressure air tube for connecting with high pressure gas equipment, the other end protrudes into degreasing tank 1 in the horizontal direction
Center.
High-pressure air tube 3 can be made to be evenly distributed in degreasing tank 1 in this way, connect pressure-air uniformly with solution
Touching.
Each high-pressure air tube 3 is uniformly arranged multiple air outlets 31 along axial direction.
Air outlet 31 is circular hole, and the diameter of air outlet 31 is 3~5mm.
The course of work of the device are as follows:
By to the solution of oil removing along the top of degreasing tank 1 be provided with oil removing before solution inlet port 11 inject, open magnetic agitation
Device 2, while high pressure gas equipment is opened, go out air along 31 high speed of air outlet of each high-pressure air tube 3, in magnetic force
Under blender 2 acts on, solution high speed rotation, air can come into full contact with the solution in degreasing tank 1, while air passes through high pressure
31 high speed ejection of air outlet of air hose 3, forms a large amount of minute bubbles, and the oil in solution rises to table on solution with bubble
Face makes the utilization rate of air be increased to 50% from 10% in this way, and since solution is in high speed rotation, drive swims in table on solution
The rotation of face oil content, and whirlpool can be formed on surface when solution rotating, it collects in oil content on medium swirl, is formed one layer very thick
, the oil-gas-water layer of small area, conducive to the separation of oil content, compared with traditional vapour floats degreasing unit, traditional oil expeller can only be
Entire solution surface forms the oil sheet of one layer of 0.1~0.2mm, and its area is big, is difficult to separate from solution, and passes through this dress
A layer thickness can be formed in the oil gas water three phase mixture of 5~10cm at the middle part of solution surface by setting, and pass through the negative of upper part
Pressure pipe siphons away, and returns to extraction plant re-using, in addition, solution is from top into lower part goes out, and oil content is that more have on top
Conducive to the separation of oil content, oil content content can be made to drop to 10mg/L from 50mg/L after oil removing.
The above, the only preferred embodiment of the utility model, are not intended to limit the protection of the utility model
Range.
Claims (9)
1. a kind of vapour floats degreasing unit, which is characterized in that described including degreasing tank, magnetic stirring apparatus and multiple high-pressure air tubes
Magnetic stirring apparatus is arranged in degreasing tank, and the multiple high-pressure air tube is uniformly plugged on the side wall of degreasing tank and is used for oil removing
Slot high pressure is passed through air driven oil content floating；The top of the degreasing tank is provided with solution inlet port before oil removing, the degreasing tank
Lower part is provided with solution discharge tube after oil removing, and the outlet of oil gas aqueous mixtures is provided at the top of the degreasing tank.
2. a kind of vapour according to claim 1 floats degreasing unit, which is characterized in that the multiple high-pressure air tube is divided into more
A high-pressure air tube group, the multiple high-pressure air tube group from the bottom of degreasing tank to degreasing tank at the top of be arranged successively.
3. a kind of vapour according to claim 2 floats degreasing unit, which is characterized in that the multiple high-pressure air tube group is equidistant
From arrangement.
4. a kind of vapour according to claim 3 floats degreasing unit, which is characterized in that each high-pressure air tube group includes
At least one high-pressure air tube, the high-pressure air tube are inserted into degreasing tank in the horizontal direction.
5. a kind of vapour according to claim 3 floats degreasing unit, which is characterized in that each high-pressure air tube group includes
Two high-pressure air tubes, described two high-pressure air tubes are symmetrically plugged in the two sides of degreasing tank.
6. a kind of vapour according to claim 4 or 5 floats degreasing unit, which is characterized in that each high-pressure air tube edge
Axially it is uniformly arranged multiple air outlets.
7. a kind of vapour according to claim 6 floats degreasing unit, which is characterized in that the diameter of the air outlet is 3
~5mm.
8. a kind of vapour according to claim 7 floats degreasing unit, which is characterized in that the oil gas aqueous mixtures are exported and born
Pressure pipe connection.
9. a kind of vapour according to claim 8 floats degreasing unit, which is characterized in that the magnetic stirring apparatus includes agitating paddle
And magnetic driver, the agitating paddle setting degreasing tank is interior and is located at the bottom of degreasing tank, and the magnetic driver setting exists
It the lower section of degreasing tank and is connect with agitating paddle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822022781.0U CN209651928U (en) | 2018-12-04 | 2018-12-04 | A kind of floating degreasing unit of vapour |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822022781.0U CN209651928U (en) | 2018-12-04 | 2018-12-04 | A kind of floating degreasing unit of vapour |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209651928U true CN209651928U (en) | 2019-11-19 |
Family
ID=68517441
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822022781.0U Active CN209651928U (en) | 2018-12-04 | 2018-12-04 | A kind of floating degreasing unit of vapour |
Country Status (1)
| Country | Link |
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| CN (1) | CN209651928U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118949484A (en) * | 2024-10-17 | 2024-11-15 | 南通新玮镍钴科技发展有限公司 | A cobalt chloride solution circulating oil removal filter tank |
-
2018
- 2018-12-04 CN CN201822022781.0U patent/CN209651928U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118949484A (en) * | 2024-10-17 | 2024-11-15 | 南通新玮镍钴科技发展有限公司 | A cobalt chloride solution circulating oil removal filter tank |
| CN118949484B (en) * | 2024-10-17 | 2024-12-20 | 南通新玮镍钴科技发展有限公司 | Cobalt chloride solution circulation deoiling and filtering tank |
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