CN202962354U - Pneumatic stirring device - Google Patents
Pneumatic stirring device Download PDFInfo
- Publication number
- CN202962354U CN202962354U CN201220706527.2U CN201220706527U CN202962354U CN 202962354 U CN202962354 U CN 202962354U CN 201220706527 U CN201220706527 U CN 201220706527U CN 202962354 U CN202962354 U CN 202962354U
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- pipeline
- chemical industry
- stirring device
- pressure vessels
- pneumatic stirring
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Abstract
The utility model relates to a pneumatic stirring device. The pneumatic stirring device comprises a chemical container containing liquid, and air source, wherein the air source is connected with the chemical container by a pipeline. The pneumatic stirring device is characterized in that an air inlet regulating switch is arranged between the air source and the chemical container through the pipeline, the pipeline is connected with the chemical container and stretches into the inner bottom wall of the chemical container, and the pipeline on the bottom wall is provided with a plurality of air outlet through holes. According to the pneumatic stirring device, the cost is reduced, the efficiency is improved, and the operation is convenient; and compared with the conventional device, the pneumatic stirring device can be used for rapidly neutralizing a precipitate within a short time.
Description
Technical field
The utility model relates to a kind of Pneumatic mixing device.
Background technology
Generally, chemical liquid contained heavy metal when static all can precipitate, and density is different, is also different to chemical property and the effect that produces, and will produce Different Effects equally.We by mechanical agitation, will affect operation before, and equipment is also easily attacked and damaged, and cost is higher.
Summary of the invention
It is good that technical problem to be solved in the utility model is to provide a kind of mixing effect, and again can be by the Pneumatic mixing device of chemical erosion.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of Pneumatic mixing device, comprise pressure vessels for the chemical industry and source of the gas that liquid is housed, described source of the gas is connected with the pressure vessels for the chemical industry pipeline, it is characterized in that, be connected with air-intaking adjusting valve by pipeline between source of the gas and pressure vessels for the chemical industry, described pipeline is connected and stretches into the interior diapire of described pressure vessels for the chemical industry with pressure vessels for the chemical industry, the pipeline on described diapire offers several and goes out vent hole.
As the further optimization of technique scheme, the described pore size that goes out vent hole is 4mm-5mm.
As the further optimization of technique scheme, the described distance that several go out between vent hole is 100mm.
The beneficial effect main manifestations of a kind of Pneumatic mixing device of the utility model is: reduces costs, raises the efficiency, and easy to operate.More traditional comparing can neutralize sediment fast in the short time.
Description of drawings
Fig. 1 is the structural representation of the utility model Pneumatic mixing device.
The specific embodiment
Below in conjunction with drawings and Examples, the utility model specific embodiment is described:
With reference to Fig. 1, a kind of Pneumatic mixing device of the present utility model, it comprises pressure vessels for the chemical industry 1 and the source of the gas 2 that liquid is housed, described source of the gas 2 is connected by pipeline 3 with pressure vessels for the chemical industry 1, be connected with air-intaking adjusting valve 4 by pipeline 3 between source of the gas 2 and pressure vessels for the chemical industry 1, described pipeline 3 is connected and stretches into the interior diapire of described pressure vessels for the chemical industry 1 with pressure vessels for the chemical industry 1, the pipeline 3 on described diapire offers a plurality of vent holes 5 that go out.
The described pore size that goes out vent hole 5 is 5mm.
The described distance that goes out between vent hole 5 is 100mm.
In the specific implementation, at first measuring vessel internal diameter size, purchase the water pipe of anti-strong acid, surrounding is fixed the acid-proof water pipe and weld in the bottom of container, then process the aperture of the 5mm of equidistant approximately 100mm on the water pipe of surrounding, link with gas source at the corner of container ejector air valve by one, liquid is poured into, open source of the gas and blow afloat by the surrounding water pipe chemical liquid of receptacle is rolled rapidly.
When the containers of 6 cubes fill with the chemical industry solutions that contains heavy metal, static through a night, all heavy metals will be deposited in container bottom, the chemical reaction effect that just can not normally play during the surperficial work of this chemical industry solutions, if the employing mechanical agitation has very many drawbacks: 1, take up room; 2, meeting strong acid easily corrodes; 3, trouble is installed; 4, cost of idleness.And in the bottom surrounding, tracheae is installed, and blow afloat by more aperture, just the sediment of bottom can be stirred rapidly.
The above has done detailed description to the utility model preferred embodiment by reference to the accompanying drawings, but the utility model is not limited to above-mentioned embodiment, in the ken that those of ordinary skills possess, can also make a variety of changes under the prerequisite that does not break away from the utility model aim.
Do not break away from design of the present utility model and scope and can make many other changes and remodeling.Should be appreciated that the utility model is not limited to specific embodiment, scope of the present utility model is defined by the following claims.
Claims (3)
1. Pneumatic mixing device, comprise pressure vessels for the chemical industry and source of the gas that liquid is housed, described source of the gas is connected with the pressure vessels for the chemical industry pipeline, it is characterized in that, be connected with air-intaking adjusting valve by pipeline between source of the gas and pressure vessels for the chemical industry, described pipeline is connected and stretches into the interior diapire of described pressure vessels for the chemical industry with pressure vessels for the chemical industry, the pipeline on described diapire offers several and goes out vent hole.
2. a kind of Pneumatic mixing device according to claim 1, is characterized in that, the described pore size that goes out vent hole is 4mm-5mm.
3. a kind of Pneumatic mixing device according to claim 1, is characterized in that, the described distance that several go out between vent hole is 100mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220706527.2U CN202962354U (en) | 2012-12-20 | 2012-12-20 | Pneumatic stirring device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220706527.2U CN202962354U (en) | 2012-12-20 | 2012-12-20 | Pneumatic stirring device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202962354U true CN202962354U (en) | 2013-06-05 |
Family
ID=48503485
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201220706527.2U Expired - Fee Related CN202962354U (en) | 2012-12-20 | 2012-12-20 | Pneumatic stirring device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202962354U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104709624A (en) * | 2014-12-09 | 2015-06-17 | 莱芜钢铁集团有限公司 | Groove bottom slag flushing structure and slag flushing method of benzene hydrogenation raw material storage tank |
| CN105771767A (en) * | 2016-03-09 | 2016-07-20 | 宁波钢铁有限公司 | Air stirring device |
| CN106422929A (en) * | 2016-08-04 | 2017-02-22 | 西北矿冶研究院 | Pneumatic catalytic stirring device and stirring method thereof |
| CN111601653A (en) * | 2018-09-06 | 2020-08-28 | 越海散装液体物流有限公司 | Flexible liquid bag with mixing member |
-
2012
- 2012-12-20 CN CN201220706527.2U patent/CN202962354U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104709624A (en) * | 2014-12-09 | 2015-06-17 | 莱芜钢铁集团有限公司 | Groove bottom slag flushing structure and slag flushing method of benzene hydrogenation raw material storage tank |
| CN104709624B (en) * | 2014-12-09 | 2017-03-15 | 莱芜钢铁集团有限公司 | Bottom land flushing cinder structure and flushing cinder method in a kind of benzene hydrogenation raw material storage tank |
| CN105771767A (en) * | 2016-03-09 | 2016-07-20 | 宁波钢铁有限公司 | Air stirring device |
| CN106422929A (en) * | 2016-08-04 | 2017-02-22 | 西北矿冶研究院 | Pneumatic catalytic stirring device and stirring method thereof |
| CN106422929B (en) * | 2016-08-04 | 2020-04-21 | 西北矿冶研究院 | Pneumatic catalytic stirring device |
| CN111601653A (en) * | 2018-09-06 | 2020-08-28 | 越海散装液体物流有限公司 | Flexible liquid bag with mixing member |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130605 Termination date: 20151220 |
|
| EXPY | Termination of patent right or utility model |