CN204996383U - It does not have mechanical transmission air agitating unit including silver -colored dead catalyst to handle - Google Patents
It does not have mechanical transmission air agitating unit including silver -colored dead catalyst to handle Download PDFInfo
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- CN204996383U CN204996383U CN201520750272.3U CN201520750272U CN204996383U CN 204996383 U CN204996383 U CN 204996383U CN 201520750272 U CN201520750272 U CN 201520750272U CN 204996383 U CN204996383 U CN 204996383U
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- compressed air
- stirred tank
- mechanical transmission
- gas collection
- dead catalyst
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- Physical Or Chemical Processes And Apparatus (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The utility model discloses an it does not have mechanical transmission air agitating unit including silver -colored dead catalyst to handle, including stirred tank, inlet pipe and gaseous rabbling mechanism, gaseous rabbling mechanism includes compressed air pipe and jet head, the inlet pipe is fixed in the stirred tank bottom and is linked together with the stirred tank, in compressed air pipe locates the inlet pipe, compressed air pipe access connection compressed air tank, the compressed air pipe export is located the export that the stirred tank just is higher than the inlet pipe, void formation feedstock channel between compressed air pipe and the inlet pipe, it is fixed with compressed air pipe's export that the jet head is located the stirred tank. The utility model discloses simple structure, convenient operation, it is sealed easy, can improve the homogeneity of stirring, the shortening reaction time, reduce the stirring energy consumption.
Description
Technical field
The utility model relates to a kind of agitating device, especially relates to a kind of process argentiferous dead catalyst mechanical transmission air stirrer.
Background technology
Argentiferous dead catalyst belongs to industrial hazard solid waste, according to the provisions of the relevant regulations issued by the State (specification is disposed in industrial dangerous waste process), needs recovery and the utilization of in line with minimizing, resource, innoxious principle, argentiferous dead catalyst being carried out to noble silver.
At present wet-leaching silver process is adopted substantially to the process of argentiferous dead catalyst.Wet-leaching generally adopts standard machinery tank diameter to carry out leaching, then is transferred in liquid by silver and then extracting silver.Mechanical agitation is generally arranged on tank diameter, the top of container or side, in order to improve the uniformity of stirring, the power that usual increase is stirred, which improves the energy consumption of stirring, requirement is added to mechanical transmission component intensity, if be arranged on the agitating device of tank diameter, container side, adds the requirement to mechanical seal.
Utility model content
The utility model is the above-mentioned technical problem existing for the mechanical agitation in order to solve prior art, provide a kind of structure simple, easy to operate, sealing easily, the uniformity stirred can be improved, Reaction time shorten, reduces the process argentiferous dead catalyst mechanical transmission air stirrer stirring energy consumption.
To achieve these goals, the utility model is by the following technical solutions:
One process argentiferous dead catalyst mechanical transmission air stirrer of the present utility model, comprise stirred tank, feed pipe and Gas Stirring mechanism, described Gas Stirring mechanism comprises compressed air hose and jet thrust, described feed pipe to be fixed on bottom stirred tank and to be connected with stirred tank, described compressed air hose is located in feed pipe, compressed air hose import connects compressed air cylinder, compressed air hose outlet is positioned at stirred tank and higher than the outlet of feed pipe, space between compressed air hose and feed pipe forms feeding-passage, the outlet that described jet thrust is positioned at stirred tank and compressed air hose is fixed.The mechanical agitation mode of the utility model abandoning tradition, compressed air hose and feed pipe form the form of sleeve pipe, space between compressed air hose and feed pipe forms feeding-passage and carries out mass transport, the material entered bottom stirred tank can be blown stirring by the gas that jet thrust sprays, rolling, thus reaches mixing effect, make bottom stirred tank without particles settling, and the oxygen in air can participate in reaction, increase chemical reaction velocity, Reaction time shorten.The utility model can improve the uniformity stirred, Reaction time shorten, reduces and stirs energy consumption.
As preferably, described jet thrust comprises gas collection plate and air jet pipe, described gas collection plate is circular plate-like shape structure, airtight gas collection cavity is provided with in gas collection plate, described compressed air hose is connected with gas collection cavity, the upper and lower wall of described gas collection cavity is equipped with some fumaroles, and described air jet pipe tilts to be fixed on outside fumarole.Air jet pipe is obliquely installed, and material is not easily entered in gas collection cavity.
As preferably, described air collecting chamber body section is in " work " font.Gas collection cavity, in " work " font, is conducive to improving the speed of compressed air ejection in gas collection cavity.
As preferably, described fumarole is interior large outer little shoulder hole.Fumarole is interior large outer little shoulder hole, can improve the pressure of compressed air ejection, improve mixing effect, make the stirring of material more even.
As preferably, the turning point of described fumarole adopts arc transition.The turning point of fumarole adopts arc transition, reduces resistance when Compressed Gas sprays from fumarole.
Therefore, the utility model has following beneficial effect: the mechanical agitation mode of the utility model abandoning tradition, compressed air hose and feed pipe form the form of sleeve pipe, space between compressed air hose and feed pipe forms feeding-passage and carries out mass transport, the material entered bottom stirred tank can be blown stirring by the gas that fumarole sprays, rolling, thus reach mixing effect, make bottom stirred tank without particles settling, and the oxygen in air can participate in reaction, increase chemical reaction velocity, Reaction time shorten.
Accompanying drawing explanation
Fig. 1 is a kind of structural representation of the present utility model.
Fig. 2 is a kind of profile of jet thrust in the utility model.
In figure: stirred tank 1, feed pipe 2, compressed air hose 3, jet thrust 4, compressed air cylinder 5, feeding-passage 6, gas collection plate 7, air jet pipe 8, gas collection cavity 9, fumarole 10.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is further described.
As Fig. 1, one process argentiferous dead catalyst mechanical transmission air stirrer shown in Fig. 2, comprise stirred tank 1, feed pipe 2 and Gas Stirring mechanism, Gas Stirring mechanism comprises compressed air hose 3 and jet thrust 4, jet thrust comprises gas collection plate 7 and air jet pipe 8, feed pipe to be fixed on bottom stirred tank and to be connected with stirred tank, compressed air hose is fixed in feed pipe, compressed air hose import connects compressed air cylinder 5, compressed air hose outlet is positioned at stirred tank and higher than the outlet of feed pipe, space between compressed air hose and feed pipe forms feeding-passage 6, the outlet that jet thrust is positioned at stirred tank and compressed air hose is fixed, gas collection plate is circular plate-like shape structure, airtight gas collection cavity 9 is provided with in gas collection plate, compressed air hose is connected with gas collection cavity, gas collection cavity upper, lower wall surface is equipped with some fumaroles 10, fumarole is interior large outer little shoulder hole, the turning point of fumarole adopts arc transition, air jet pipe tilts to be fixed on outside fumarole.
When material is pressed into stirred tank through feeding-passage 6, stirring is blown to the material of stirred tank through the compressed air of air jet pipe ejection in jet thrust simultaneously, material is rolled up and down, along with air rises, thus reach mixing effect, make without particles settling bottom stirred tank, and the oxygen in air can participate in reaction, increase chemical reaction velocity, Reaction time shorten.The utility model structure is simple, easy to operate, and sealing easily, can improve the uniformity stirred, Reaction time shorten, reduces and stirs energy consumption.
Claims (5)
1. a process argentiferous dead catalyst mechanical transmission air stirrer, it is characterized in that, comprise stirred tank (1), feed pipe (2) and Gas Stirring mechanism, described Gas Stirring mechanism comprises compressed air hose (3) and jet thrust (4), described feed pipe to be fixed on bottom stirred tank and to be connected with reactor, described compressed air hose is located in feed pipe, compressed air hose import connects compressed air cylinder (5), compressed air hose outlet is positioned at reactor and higher than the outlet of feed pipe, space between compressed air hose and feed pipe forms feeding-passage (6), the outlet that described jet thrust is positioned at stirred tank and compressed air hose is fixed.
2. one process argentiferous dead catalyst mechanical transmission air stirrer according to claim 1, it is characterized in that, described jet thrust comprises gas collection plate (7) and air jet pipe (8), described gas collection plate is circular plate-like shape structure, airtight gas collection cavity (9) is provided with in gas collection plate, described compressed air hose is connected with gas collection cavity, and the upper and lower wall of described gas collection cavity is equipped with some fumaroles (10), and described air jet pipe tilts to be fixed on outside fumarole.
3. one process argentiferous dead catalyst mechanical transmission air stirrer according to claim 2, it is characterized in that, described air collecting chamber body section is in " work " font.
4. one process argentiferous dead catalyst mechanical transmission air stirrer according to claim 2, it is characterized in that, described fumarole is interior large outer little shoulder hole.
5. one process argentiferous dead catalyst mechanical transmission air stirrer according to claim 4, it is characterized in that, the turning point of described fumarole adopts arc transition.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520750272.3U CN204996383U (en) | 2015-09-25 | 2015-09-25 | It does not have mechanical transmission air agitating unit including silver -colored dead catalyst to handle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520750272.3U CN204996383U (en) | 2015-09-25 | 2015-09-25 | It does not have mechanical transmission air agitating unit including silver -colored dead catalyst to handle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204996383U true CN204996383U (en) | 2016-01-27 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201520750272.3U Active CN204996383U (en) | 2015-09-25 | 2015-09-25 | It does not have mechanical transmission air agitating unit including silver -colored dead catalyst to handle |
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| CN (1) | CN204996383U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106076181A (en) * | 2016-08-22 | 2016-11-09 | 科威嘉粉末涂料（天津）股份有限公司 | A kind of metal powder coating production mixing arrangement |
| CN110575779A (en) * | 2019-09-29 | 2019-12-17 | 云南大红山管道有限公司 | Novel slurry stirring device |
| CN112827434A (en) * | 2020-12-24 | 2021-05-25 | 内蒙古华镒环境工程有限公司 | Efficient recovery device and recovery method for lead-silver slag |
-
2015
- 2015-09-25 CN CN201520750272.3U patent/CN204996383U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106076181A (en) * | 2016-08-22 | 2016-11-09 | 科威嘉粉末涂料（天津）股份有限公司 | A kind of metal powder coating production mixing arrangement |
| CN110575779A (en) * | 2019-09-29 | 2019-12-17 | 云南大红山管道有限公司 | Novel slurry stirring device |
| CN112827434A (en) * | 2020-12-24 | 2021-05-25 | 内蒙古华镒环境工程有限公司 | Efficient recovery device and recovery method for lead-silver slag |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 314300, No. 1, Donggang Road, Hangzhou Bay Bridge, Haiyan County, Zhejiang, Jiaxing Patentee after: Zhejiang Teli renewable resources Co., Ltd Address before: 314300, No. 1, Donggang Road, Hangzhou Bay Bridge, Haiyan County, Zhejiang, Jiaxing Patentee before: ZHEJIANG TELI RECYCLING RESOURCES Co.,Ltd. |