CN203546123U - Agitating tank with high-pressure blast nozzles - Google Patents
Agitating tank with high-pressure blast nozzles Download PDFInfo
- Publication number
- CN203546123U CN203546123U CN201320798959.5U CN201320798959U CN203546123U CN 203546123 U CN203546123 U CN 203546123U CN 201320798959 U CN201320798959 U CN 201320798959U CN 203546123 U CN203546123 U CN 203546123U
- Authority
- CN
- China
- Prior art keywords
- nozzle
- agitating tank
- pressure
- tank
- pressure air
- 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
- 229910000831 Steel Inorganic materials 0.000 claims description 17
- 239000010959 steel Substances 0.000 claims description 17
- 210000002421 cell wall Anatomy 0.000 claims description 3
- 239000000463 material Substances 0.000 abstract description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 5
- 239000001301 oxygen Substances 0.000 abstract description 5
- 229910052760 oxygen Inorganic materials 0.000 abstract description 5
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 230000003247 decreasing effect Effects 0.000 abstract 1
- 238000004134 energy conservation Methods 0.000 abstract 1
- 238000005272 metallurgy Methods 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 241000405070 Percophidae Species 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000009854 hydrometallurgy Methods 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000021715 photosynthesis, light harvesting Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
Abstract
The utility model discloses an agitating tank with high-pressure blast nozzles and belongs to mixing equipment of the metallurgy industry. The agitating tank with high-pressure blast nozzles is characterized in that a high-pressure air tube is installed every 120-degree angle at the position inside the agitating tank, close to cylindrical tank wall, and a nozzle is connected to the lower end of each high-pressure air tube. Each nozzle is installed at a height lower than a mixer impeller, and the distance between each nozzle and the bottom of the agitating tank is more than or equal to 400 mm. The nozzles at the lower end of the high-pressure air tubes are respectively connected to the corresponding air tube through a connector. The structure of each nozzle is that a spoon-shaped cambered surface is connected to the outside of an air outlet. The agitating tank is additionally provided with nozzles, therefore, compressed air can be utilized more efficiently, the consumption of compressed air can be decreased by about 35%, and meanwhile, the load of a mixing device can be reduced, and the oxygen supply for the material at the bottom can be increased. The agitating tank with high-pressure blast nozzles greatly reduces energy consumption of equipment and achieves the purpose of energy conservation and efficiency enhancement.
Description
Technical field: the utility model relates to the mix and blend equipment of smelter, particularly a kind of steel basin.
Background technology: the smelting enterprise of metallurgical mine and employing hydrometallurgy uses groove tank whipping device more, in the middle of existing production, the pipe that utilizes head to flatten into duckbill is input to pressurized air in steel basin tank, enhance productivity and leaching yield, coordinate whipping appts that material is uniformly distributed.Use compressed-air actuated object to be: to increase the oxygen element in material, improve disperse and distribute, strengthen contact area, be conducive to the conversion reaction between material.Along with the increasing of turnout, larger to compression use gas usage quantity, by annual data are adjusted, the effective rate of utilization of wind is lower, causes energy dissipation comparatively serious, and production efficiency is low.
Summary of the invention: the purpose of this utility model is a kind of steel basin with high-pressure blast nozzle of design, improve the utilization ratio of wind, increase the oxygen amount in material, accelerate the conversion of material inside, the shortened process time, the purpose of this utility model is achieved in that the steel basin with high-pressure blast nozzle, comprises steel basin tank, agitator and high-pressure air hose.In steel basin tank, near cylindrical cell wall place, at interval of 120 degree angles, a high-pressure air hose is housed, high-pressure air hose lower end connects nozzle, and nozzle mounting height is under agitator paddle, apart from groove pot bottom >=400mm.The nozzle of high-pressure air hose lower end is connected with airduct by joint, and the structure of nozzle is to connect a spoon-shaped cambered surface in air outlet outside.
From result of use, steel basin has installed nozzle additional, has improved compressed-air actuated effective rate of utilization, reduces pressurized air and consumes 35% left and right.Can reduce the load of whipping appts again, greatly reduce equipment energy consumption, reached the object of energy efficiency simultaneously.According to production practical application, the flow of having stopped using is at present 80Nm
3the equipment of/min non-lubricated compressor and a set of small-sized oxygen generation system, annual expense of saving is more than 1,000,000 yuan.
Accompanying drawing explanation: Fig. 1 is the structural representation with the steel basin of high-pressure blast nozzle.Fig. 2 is the structural representation of nozzle.Fig. 3 is the sectional view of Fig. 2, represents the air outlet of nozzle and being connected of spoon-shaped cambered surface.
Embodiment: be described further below in conjunction with accompanying drawing.
With the steel basin of high-pressure blast nozzle, comprise steel basin tank, agitator and high-pressure air hose.At steel basin tank 1 center, there is agitator 3, in steel basin tank, near cylindrical cell wall place, at interval of 120 degree angles, a high-pressure air hose 2 is housed, high-pressure air hose lower end connects nozzle 4, and nozzle mounting height is under agitator paddle, apart from groove pot bottom >=400mm, reduce washing away groove pot bottom.Air-flow by nozzle makes material produce motion, effectively reduces agitator motor load, increases the dispersity of material, and the utilization ratio of oxygen in material is improved, and accelerates the chemical reaction of storeroom.The nozzle 4 of high-pressure air hose lower end is connected with airduct by joint 5, and the structure of nozzle is that air outlet 7 outsides connect a spoon-shaped cambered surface 6.Reflection and diffusing air current, change air supply pattern in the past, effectively improves the utilization of wind, reduced energy loss.
Claims (2)
1. with the steel basin of high-pressure blast nozzle, comprise steel basin tank, agitator and high-pressure air hose, it is characterized in that: in steel basin tank (1), near cylindrical cell wall place, at interval of 120 degree angles, a high-pressure air hose (2) is housed, high-pressure air hose lower end connects nozzle (4), nozzle mounting height is under agitator paddle, apart from groove pot bottom >=400mm.
2. the steel basin with high-pressure blast nozzle as claimed in claim 1, it is characterized in that: the nozzle of high-pressure air hose lower end (4) is connected with airduct by joint (5), the structure of nozzle is to connect a spoon-shaped cambered surface (6) in air outlet (7) outside.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320798959.5U CN203546123U (en) | 2013-11-28 | 2013-11-28 | Agitating tank with high-pressure blast nozzles |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320798959.5U CN203546123U (en) | 2013-11-28 | 2013-11-28 | Agitating tank with high-pressure blast nozzles |
Publications (1)
Publication Number | Publication Date |
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CN203546123U true CN203546123U (en) | 2014-04-16 |
Family
ID=50464268
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201320798959.5U Expired - Lifetime CN203546123U (en) | 2013-11-28 | 2013-11-28 | Agitating tank with high-pressure blast nozzles |
Country Status (1)
Country | Link |
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CN (1) | CN203546123U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104120251A (en) * | 2014-07-25 | 2014-10-29 | 河北钢铁股份有限公司承德分公司 | Hydrometallurgy reactor and hydrometallurgy method capable of improving target element leaching rate |
CN105592904A (en) * | 2013-09-27 | 2016-05-18 | 加拿大思博选矿设备公司 | Method and apparatus for liquid/solid separation such as dewatering particulate solids and agitation leaching |
-
2013
- 2013-11-28 CN CN201320798959.5U patent/CN203546123U/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105592904A (en) * | 2013-09-27 | 2016-05-18 | 加拿大思博选矿设备公司 | Method and apparatus for liquid/solid separation such as dewatering particulate solids and agitation leaching |
CN104120251A (en) * | 2014-07-25 | 2014-10-29 | 河北钢铁股份有限公司承德分公司 | Hydrometallurgy reactor and hydrometallurgy method capable of improving target element leaching rate |
CN104120251B (en) * | 2014-07-25 | 2016-08-17 | 河北钢铁股份有限公司承德分公司 | Improve object element and turn hydrometallurgy reactor and the Wet-process metallurgy method of leaching rate |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CX01 | Expiry of patent term |
Granted publication date: 20140416 |
|
CX01 | Expiry of patent term |