CN204017626U - A kind of hydrometallurgic recovery gas device - Google Patents
A kind of hydrometallurgic recovery gas device Download PDFInfo
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- CN204017626U CN204017626U CN201420496815.9U CN201420496815U CN204017626U CN 204017626 U CN204017626 U CN 204017626U CN 201420496815 U CN201420496815 U CN 201420496815U CN 204017626 U CN204017626 U CN 204017626U
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Abstract
The utility model provides a kind of hydrometallurgic recovery gas device, comprise pure water tank, ejector, blending tank, condenser, cooling tank and diversion cans, the outlet of pure water tank is connected with the lower inlet of ejector by the first pipeline, the outlet of ejector is connected with the air inlet of blending tank by second pipe, the lower part outlet of blending tank is connected with the import of condenser by the 3rd pipeline, the outlet of condenser is connected with the import of cooling tank by the 4th pipeline, and the outlet of cooling tank is connected with diversion cans import by the 5th pipeline; The horizontal inlet of ejector is connected with steam pipe, and blending tank sidepiece is provided with offgas duct.The beneficial effects of the utility model reduce environmental pollution, and organic gas is recycled, cost-saving; Do not adopt other organic solvent, save recovery and the processing cost of other solvent.
Description
Technical field
The utility model belongs to gas recovery techniques field, especially relates to a kind of hydrometallurgic recovery gas device.
Background technology
Some the organic gas boiling points used in industrial production are low, volatile, water insoluble, and normal adjoint tail gas is discharged in air, not only causes serious pollution to environment, and adds production cost, bring very large puzzlement to the production of company.
For the recovery of organic solvent, other organic solvent of normal employing absorbs it, although this kind of method reduces the pollution of organic solvent to air, in operation cost, turn increase the cost of other organic solvent, the separation costs of two kinds of organic solvents and the processing cost of waste liquid.
Summary of the invention
The purpose of this utility model is to provide a kind of hydrometallurgic recovery gas device, can reduce environmental pollution, and organic gas is recycled, cost-saving; Do not adopt other organic solvent, save recovery and the processing cost of other solvent.
For solving the problems of the technologies described above, the technical solution adopted in the utility model is: a kind of hydrometallurgic recovery gas device, comprise pure water tank, ejector, blending tank, condenser, cooling tank and diversion cans, it is characterized in that: the outlet of pure water tank is connected with the lower inlet of ejector by the first pipeline, the outlet of ejector is connected with the air inlet of blending tank by second pipe, the lower part outlet of blending tank is connected with the import of condenser by the 3rd pipeline, the outlet of condenser is connected with the import of cooling tank by the 4th pipeline, the outlet of cooling tank is connected with diversion cans import by the 5th pipeline, the horizontal inlet of ejector is connected with steam pipe, and blending tank sidepiece is provided with offgas duct.
Preferably, steam jet, tail gas nozzle and deflector is provided with in described blending tank.
Preferably, described deflector is semicircle.
The advantage that the utility model has and good effect are: owing to adopting technique scheme, can reduce environmental pollution, organic gas is recycled, cost-saving; Do not adopt other organic solvent, save recovery and the processing cost of other solvent.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the sectional view of the utility model blending tank.
In figure: 1, pure water tank; 2, ejector; 3, blending tank; 4, condenser; 5, cooling tank; 6, diversion cans; 7, steam pipe; 8, the first pipeline; 9, second pipe; 10, air inlet; 11, offgas duct; 12, the 3rd pipeline; 13, the 4th pipeline; 14, the 5th pipeline; 31, tail gas nozzle; 32, steam jet; 33, deflector.
Detailed description of the invention
As shown in Figure 1, the utility model provides a kind of hydrometallurgic recovery gas device, comprise pure water tank 1, ejector 2, blending tank 3, condenser 4, cooling tank 5 and diversion cans 6, the outlet of pure water tank 1 is connected with the lower inlet of ejector 2 by the first pipeline 8, the outlet of ejector 2 is connected by the air inlet of second pipe 9 with blending tank 3, the lower part outlet of blending tank 3 is connected with the import of condenser 4 by the 3rd pipeline 12, the outlet of condenser 4 is connected with the import of cooling tank 5 by the 4th pipeline 13, the outlet of cooling tank 5 is connected with diversion cans 6 import by the 5th pipeline 14, the horizontal inlet of ejector 2 is connected with steam pipe 7, and blending tank 3 sidepiece is provided with offgas duct 11.
The effect of blending tank 3 allows Low Temperature Steam wrap up in mix organic gas tail gas, be provided with steam jet 32, tail gas nozzle 31 and deflector 33 in blending tank 3, being to allow Low Temperature Steam and organic gas tail gas fully mix.
Preferably, deflector 33 is semicircle.
In the present embodiment, ejector 2 has two imports, and lower inlet is suction chamber import, and upper inlet is jet import.The operation principle of ejector: under impeller of pump High Rotation Speed, liquid sprays from nozzle with high speed, when swiftly flowing liquid is by suction chamber, vacuum can be formed at suction chamber, suck large quantity of air by wireway, after air enters mixing chamber, at trunnion, place acutely mixes with liquid, forms gas liquid mixture, is discharged by anemostat, air rises with fine gas bubbles in water body, in whole process, form efficient material Transfer.Can carry out disinfection to sewage, purification.
The present embodiment adopts high-temperature steam to form jet, forms vacuum at suction chamber, and suck the water in pure water tank 1 by the first pipeline, steam mixes with pure water, and pure water is vaporizated into Low Temperature Steam by steam, increases quantity of steam, and pure water is lowered the temperature to high-temperature steam simultaneously.
The course of work of this example: during use, high-temperature steam enters ejector 2 by steam pipe 7, water in pure water tank 1 enters ejector 2 through the first pipeline 8 and vaporizes, Low Temperature Steam enters in blending tank 3 from ejector 2 by second pipe 9, the tail gas entered through offgas duct 11 mixes with Low Temperature Steam, mixed gas enters condenser 4 through the 3rd pipeline 12 and carries out condensation, the condensate liquid that condensation obtains enters cooling tank 5 and cools further, and cooled liquid enters diversion cans 6 and carries out separatory and storage.
Owing to adopting technique scheme, can environmental pollution be reduced, organic gas is recycled, cost-saving; Do not adopt other organic solvent, save recovery and the processing cost of other solvent.
Above embodiment of the present utility model has been described in detail, but described content being only preferred embodiment of the present utility model, can not being considered to for limiting practical range of the present utility model.All equalizations done according to the utility model application range change and improve, and all should still belong within patent covering scope of the present utility model.
Claims (3)
1. a hydrometallurgic recovery gas device, comprise pure water tank, ejector, blending tank, condenser, cooling tank and diversion cans, it is characterized in that: the outlet of pure water tank is connected with the lower inlet of ejector by the first pipeline, the outlet of ejector is connected with the air inlet of blending tank by second pipe, the lower part outlet of blending tank is connected with the import of condenser by the 3rd pipeline, the outlet of condenser is connected with the import of cooling tank by the 4th pipeline, and the outlet of cooling tank is connected with diversion cans import by the 5th pipeline; The horizontal inlet of ejector is connected with steam pipe, and blending tank sidepiece is provided with offgas duct.
2. a kind of hydrometallurgic recovery gas device according to claim 1, is characterized in that: be provided with steam jet, tail gas nozzle and deflector in described blending tank.
3. a kind of hydrometallurgic recovery gas device according to claim 2, is characterized in that: described deflector is for semicircle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420496815.9U CN204017626U (en) | 2014-09-01 | 2014-09-01 | A kind of hydrometallurgic recovery gas device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420496815.9U CN204017626U (en) | 2014-09-01 | 2014-09-01 | A kind of hydrometallurgic recovery gas device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204017626U true CN204017626U (en) | 2014-12-17 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420496815.9U Expired - Fee Related CN204017626U (en) | 2014-09-01 | 2014-09-01 | A kind of hydrometallurgic recovery gas device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204017626U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104874198A (en) * | 2015-04-10 | 2015-09-02 | 顾卫荣 | Condensable gaseous substance recycling method and condensable gaseous substance recycling system suitable for tail gas and exhaust gas |
-
2014
- 2014-09-01 CN CN201420496815.9U patent/CN204017626U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104874198A (en) * | 2015-04-10 | 2015-09-02 | 顾卫荣 | Condensable gaseous substance recycling method and condensable gaseous substance recycling system suitable for tail gas and exhaust gas |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141217 Termination date: 20160901 |