CN202933507U - Device for recycling gas by using wet method - Google Patents
Device for recycling gas by using wet method Download PDFInfo
- Publication number
- CN202933507U CN202933507U CN 201220665844 CN201220665844U CN202933507U CN 202933507 U CN202933507 U CN 202933507U CN 201220665844 CN201220665844 CN 201220665844 CN 201220665844 U CN201220665844 U CN 201220665844U CN 202933507 U CN202933507 U CN 202933507U
- Authority
- CN
- China
- Prior art keywords
- tank
- pipeline
- outlet
- condenser
- inlet
- 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.)
- Expired - Lifetime
Links
Images
Abstract
The utility model discloses a device for recycling gas by using a wet method. The device comprises a pure water tank, a jet device, a mixing tank, a condenser and a cooling tank, wherein an outlet of the pure water tank is communicated with a lower inlet of the jet device through a first pipeline, an outlet of the jet device is communicated with an air inlet of the mixing tank through a second pipeline, a lower outlet of the mixing tank is communicated with an inlet of the condenser through a third pipeline, an outlet of the condenser is communicated with an inlet of the cooling tank through a fourth pipeline, a level inlet of the jet device is communicated with a steam pipe, and a tail gas pipe is arranged at the upper part of the mixing tank which is provided with a steam nozzle, a tail gas nozzle and a deflector; and the deflector is semicircular. The utility model provides a method for recycling an organic solvent in tail gas, thereby reducing the environmental pollution, recycling organic gas, saving the cost; other organic solvents are not used, thereby saving the recycling and treatment cost of the other organic solvents.
Description
Technical field
The utility model relates to the device that gas reclaims, especially a kind of hydrometallurgic recovery gas device.
Background technology
Some organic gas boiling points that use in industrial production are low, volatile, water insoluble, often follow tail gas to be discharged in air, not only environment caused serious pollution, and increased production cost, bring very large puzzlement for the production of company.
Recovery for organic solvent, normal other organic solvent that adopts absorbs it, although this kind method has reduced the pollution of organic solvent to air, the separation costs of the cost of other organic solvent, two kinds of organic solvents and the processing cost of waste liquid have been increased again in operation cost.
The utility model content
The technical problems to be solved in the utility model is to provide a kind of hydrometallurgic recovery gas device, and a kind of method that reclaims organic solvent in tail gas is provided, and has reduced environmental pollution, and that organic gas obtains is recycling, saves cost; Do not adopt other organic solvent, saved recovery and the processing cost of other solvent.
Technical solution adopted in the utility model is:
A kind of hydrometallurgic recovery gas device comprises pure water tank, ejector, blending tank, condenser and cooling tank; 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, and the outlet of condenser is connected with the import of cooling tank by the 4th pipeline;
The horizontal inlet of ejector is connected with steam pipe, and blending tank top is provided with offgas duct.
Be provided with steam jet, tail gas nozzle and deflector in blending tank.
Deflector is semicircle.
Ejector operation principle: under the impeller of pump High Rotation Speed, liquid sprays from nozzle with high speed, when swiftly flowing liquid passes through suction chamber, can form vacuum at suction chamber, suck large quantity of air by wireway, after air enters mixing chamber, the place is acutely mixed with liquid at trunnion, forms gas liquid mixture, is discharged by anemostat, air rises with trickle bubble in water body, forms efficient material Transfer in whole process.Can carry out disinfection to sewage, purify.
Ejector has two imports, and lower inlet is the suction chamber import, and upper inlet is the jet import.
The utility model adopts high-temperature steam to form jet, forms vacuum at suction chamber, and by the water in the first pipeline suction pure water tank, steam mixes with pure water, and steam is vaporizated into Low Temperature Steam with pure water, increases quantity of steam, and pure water is lowered the temperature to high-temperature steam simultaneously.
The effect of blending tank allows Low Temperature Steam wrap up in and is mixed with machine gas tail gas, and it is in order to allow Low Temperature Steam and organic gas tail gas fully mix that tail gas nozzle, steam jet and deflector are set.
The beneficial effect that adopts technique scheme to produce is:
1. the utility model provides a kind of method that reclaims organic solvent in tail gas, has reduced environmental pollution, and that organic gas obtains is recycling, saves cost; Do not adopt other organic solvent, saved recovery and the processing cost of other solvent.
2. adopt high-temperature steam vaporization pure water to obtain Low Temperature Steam, reduced the steam use amount, alleviated the condenser burden, reduced cost.
3. tail gas nozzle, steam jet and deflector are set in blending tank, steam and tail gas are fully mixed.
The utility model simple in structure, be easy to realize to have good practicality and promotional value.
Description of drawings
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the complete section figure of blending tank in Fig. 1.
The specific embodiment
A kind of hydrometallurgic recovery gas device comprises pure water tank 1, ejector 2, blending tank 3, condenser 4 and cooling tank 5; The outlet of pure water tank 1 is connected with the lower inlet of ejector 2 by the first pipeline 13, the outlet of ejector 2 is connected with the air inlet 8 of blending tank 3 by second pipe 7, the lower part outlet of blending tank 3 is connected with the import of condenser 4 by the 3rd pipeline 11, and the outlet of condenser 4 is connected with the import of cooling tank 5 by the 4th pipeline 12;
The horizontal inlet of ejector 2 is connected with steam pipe 6, and blending tank 3 tops are provided with offgas duct 10.
Be provided with steam jet 14, tail gas nozzle 9 and deflector 15 in blending tank 3.
Deflector 15 is semicircle.
During use, high-temperature steam enters ejector 2 by steam pipe 6, water in pure water tank 1 enters ejector through the first pipeline 13 and vaporizes, Low Temperature Steam is entered in blending tank 3 by second pipe 7 from ejector 2, the tail gas that enters through offgas duct 10 mixes with Low Temperature Steam, mixed gas enters condenser 4 through the 3rd pipeline 11 and carries out condensation, and the condensate liquid that condensation obtains enters cooling tank 5 and further carries out cooling, separatory and storage.
Claims (3)
1. a hydrometallurgic recovery gas device, is characterized in that comprising pure water tank (1), ejector (2), blending tank (3), condenser (4) and cooling tank (5); The outlet of pure water tank (1) is connected by the lower inlet of the first pipeline (13) with ejector (2), the outlet of ejector (2) is connected with the air inlet (8) of blending tank (3) by second pipe (7), the lower part outlet of blending tank (3) is connected by the import of the 3rd pipeline (11) with condenser (4), and the outlet of condenser (4) is connected by the import of the 4th pipeline (12) with cooling tank (5);
The horizontal inlet of ejector (2) is connected with steam pipe (6), and blending tank (3) top is provided with offgas duct (10).
2. a kind of hydrometallurgic recovery gas device according to claim 1, is characterized in that being provided with in described blending tank (3) steam jet (14), tail gas nozzle (9) and deflector (15).
3. a kind of hydrometallurgic recovery gas device according to claim 2, is characterized in that described deflector (15) is for semicircle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220665844 CN202933507U (en) | 2012-12-06 | 2012-12-06 | Device for recycling gas by using wet method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220665844 CN202933507U (en) | 2012-12-06 | 2012-12-06 | Device for recycling gas by using wet method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202933507U true CN202933507U (en) | 2013-05-15 |
Family
ID=48317769
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220665844 Expired - Lifetime CN202933507U (en) | 2012-12-06 | 2012-12-06 | Device for recycling gas by using wet method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202933507U (en) |
Cited By (2)
| 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 |
| CN109621597A (en) * | 2019-01-25 | 2019-04-16 | 江苏师范大学 | Dedusting and purifying air system |
-
2012
- 2012-12-06 CN CN 201220665844 patent/CN202933507U/en not_active Expired - Lifetime
Cited By (2)
| 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 |
| CN109621597A (en) * | 2019-01-25 | 2019-04-16 | 江苏师范大学 | Dedusting and purifying air system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103936569B (en) | A kind of high-concentration methylal production technique apparatus and method | |
| CN202933507U (en) | Device for recycling gas by using wet method | |
| CN204017626U (en) | A kind of hydrometallurgic recovery gas device | |
| CN204034517U (en) | A kind of waste gas purification apparatus for making fish meal | |
| CN202682821U (en) | Ethyl acetate solvent recovery device | |
| CN203861954U (en) | Removing and recycling system for solvents | |
| CN201470141U (en) | Tail gas recovery device | |
| CN203447924U (en) | Waste gas treating device | |
| CN204356097U (en) | For the treatment of the system of paper-making pulping waste water | |
| CN204159066U (en) | Chemical volatility gas discharging retracting device | |
| CN203620499U (en) | Waste gas treatment system | |
| CN203303822U (en) | Recovery device of ethanol tail gas | |
| CN207871586U (en) | A kind of garbage loading embeading biogas level-one steam-water separator | |
| CN202961916U (en) | Calcium lactate concentration device | |
| CN205965438U (en) | Methanol recovery device | |
| CN202465363U (en) | Low pressure oxygenation jet apparatus | |
| CN207196985U (en) | A kind of circulating cooling-water machine | |
| CN205575699U (en) | Multitube efflux formula dive aeration machine | |
| CN203625114U (en) | Garbage leachate high efficient aerator | |
| CN203316124U (en) | Organic silicon adhesive production line | |
| CN204159181U (en) | A kind of cold-rolling pickling line acid mist reclaims circulation without tapping equipment | |
| CN204261673U (en) | Aliphatic water reducing agent preparation facilities | |
| CN202342939U (en) | Alcohol secondary recovering tower | |
| CN203938566U (en) | A kind of printing-dying wastewater recycling and sludge drying treatment equipment | |
| CN203878082U (en) | High-concentration methylal production process device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 052165 Shijiazhuang economic and Technological Development Zone (good village) Jinsha Road, Hebei Patentee after: HEBEI HAILI FRAGRANCES CO.,LTD. Address before: 052165 Shijiazhuang economic and Technological Development Zone (good village) Jinsha Road, Hebei Patentee before: Shijiazhuang Haili-Fine Chemical Co.,Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130515 |