CN201823495U - Gas-filling stirring device - Google Patents
Gas-filling stirring device Download PDFInfo
- Publication number
- CN201823495U CN201823495U CN2010205367599U CN201020536759U CN201823495U CN 201823495 U CN201823495 U CN 201823495U CN 2010205367599 U CN2010205367599 U CN 2010205367599U CN 201020536759 U CN201020536759 U CN 201020536759U CN 201823495 U CN201823495 U CN 201823495U
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- Prior art keywords
- gas
- stirring device
- rotor
- main shaft
- filling
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- Expired - Fee Related
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- 238000003756 stirring Methods 0.000 title claims abstract description 25
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 239000000203 mixture Substances 0.000 claims description 8
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 claims description 3
- 239000002002 slurry Substances 0.000 abstract description 7
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 239000000126 substance Substances 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 238000005272 metallurgy Methods 0.000 abstract description 3
- 238000005520 cutting process Methods 0.000 abstract description 2
- 238000002360 preparation method Methods 0.000 abstract description 2
- 239000002351 wastewater Substances 0.000 abstract description 2
- 238000003889 chemical engineering Methods 0.000 abstract 1
- 230000001804 emulsifying effect Effects 0.000 abstract 1
- 238000002156 mixing Methods 0.000 description 6
- 230000006641 stabilisation Effects 0.000 description 6
- 238000011105 stabilization Methods 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- 230000033228 biological regulation Effects 0.000 description 3
- 230000036632 reaction speed Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000004087 circulation Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000005273 aeration Methods 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The utility model discloses a gas-filling stirring device comprising a motor (1) and a main shaft (2), wherein one end of the main shaft (2) is connected with the output end of the motor (1), and the other end is provided with a rotor (3) which is provided with a gas-liquid mixed body flow guiding port (4); and rectangular air cutting sawteeth (5) are vertically arranged below the rotor (3) in a cross shape. In the gas-filling stirring device, the structure is simple, the stirring function, the gas filling function and functions of emulsifying bubbles, prolonging the overflowing path of the bubbles and forming various circulating collision road by liquid are integrated into a whole, the strong collision of all parts of the slurry is guaranteed, the air utilization rate is improved, and the energy consumption is greatly saved. The gas-filling stirring device can be widely applied in the industrial fields of metallurgy, chemical engineering, environmental protection and the like, and is particularly applicable to application of oxygenated treatment of waste water, slurry preparation of a floatation factory and reactors of chemical products.
Description
Technical field
The utility model relates to a kind of agitating device, especially relate to a kind of inflating and stirring device that contains motor, main shaft and rotor, can be in industrial circle extensive uses such as metallurgy, chemical industry, environmental protection, be applicable to especially that the waste water oxygenation is handled, use in the reactor of flotation mill's pulp preparation and chemical products.
Background technology
In the industrial production in fields such as metallurgy, chemical industry, environmental protection, usually need slurry stirring device, using more is the vane type agitating device.Chinese patent ZL200820124070 discloses a kind of vane type agitating device, its structure comprises a vertical shaft and the several layers impeller of fixed interval on shaft vertically, the mode that impeller does not have key, taper seat and key or taper seat and do not have key by the face of cylinder and key or the face of cylinder is fixed on the shaft, be fixed on the several layers impeller on the shaft, the blade rotation direction of adjacent impeller is identical or opposite, make load not only produce strong radially and tangential motion, also produce strong axial convective motion, thereby the reinforcement whipping process improves stirring efficiency.The high strength that this agitating device is suitable for mixing plant slurries such as flowsheet of slurry agitation grinding machine, tank diameter stirs.But this agitating device does not possess the inflation frothing function, when slurry needs a large amount of air to react with it, because the bubble generation is few, thereby caused the reaction speed of the stage of reaction slow, outstanding problem such as air utilization ratio is low, production equipment efficient is utilized low, energy consumption height.
Chinese patent ZL200920096955 discloses a kind of aerated inflating and stirring device, it is to be made of inlet duct, feed arrangement and agitating device, wherein: inlet duct is made of gas transfer pipeline, pressure regulation filter, voltage stabilization and current stabilization metering device, one end of gas transfer pipeline connects compressed air, the pressure regulation filter is installed on the gas transfer pipeline, the outlet of pressure regulation filter connects the voltage stabilization and current stabilization metering device, and the outlet of voltage stabilization and current stabilization metering device connects the gas feed of a pre-mixing apparatus by a non-return valve; The discharging opening of feed arrangement is connected with the slurry import of pre-mixing apparatus, and the compound outlet of this pre-mixing apparatus is connected with the charging aperture of agitating device, and this agitating device is a pipeline high shear mixing emulsifier unit.This device has foaming, stirs dual-use function, but the device structure complexity, member is many, price is high, processing, installs inconveniently, and production capacity is limited.
Summary of the invention
The purpose of this utility model is exactly at the above-mentioned problems in the prior art, and provide a kind of simple in structure, frothing percentage is high, reaction speed is fast, air utilization ratio is high, device efficiency is high, the few inflating and stirring device of power consumption.Outstanding problems such as it improves by the agitating device to existing consersion unit, and the reaction speed that solves the stage of reaction is slow, air utilization ratio is low, production equipment efficient is utilized low, energy consumption height.
For reaching above-mentioned purpose of the present utility model, a kind of inflating and stirring device of the utility model by the following technical solutions:
A kind of inflating and stirring device of the utility model comprises motor, main shaft, and an end of main shaft links to each other with the output of motor, at the other end of main shaft rotor is installed, and rotor is provided with the gas liquid mixture flow-guiding mouth, is provided with the air gulleting below the rotor.
Described rotor is discoid, and the gas liquid mixture flow-guiding mouth which is provided with evenly is provided with along the disc face of rotor; Described air gulleting is a rectangle, be " ten " word shape be vertically set on rotor below.
The height of described air gulleting is 6～10 millimeters and is advisable; The diameter of described gas liquid mixture flow-guiding mouth and the diameter of rotor ratio are 1: 9～12 for good; Max line cutting speed 12 meter per seconds of described rotor, rotating speed is 900～1100 rev/mins.
After a kind of inflating and stirring device of the utility model adopts above technical scheme, have following beneficial effect:
(1) simple in structure, processing, easy for installation.
(2) gas distribution is even, and air-flow forms countless micro bubbles when the bump wall, thereby air is fully mixed with various components, has shortened mixing time, and air is dissolved in the water in large quantities, has improved treatment effeciency.
(2) collection agitating function, aerification function and emulsification bubble, prolongation bubble overflow path and liquid form function and one such as various circulations collision roads, have guaranteed the fierce collision of slip each several part to have improved air utilization ratio.
(3) utilize the utility model inflating and stirring device, under the constant situation of original technology, make and produce reaction time shortening 30%-50%, saved energy consumption greatly, and can under the situation that does not increase investment, make the production production capacity improve 1.5 times.
Description of drawings
Fig. 1 is the structural nexus schematic diagram of a kind of inflating and stirring device of the utility model;
Fig. 2 be among Fig. 1 along A-A to the plan structure schematic diagram
The specific embodiment
For further describing the utility model, a kind of inflating and stirring device of the utility model is further described below in conjunction with embodiment.
Referring to Fig. 1, Fig. 2, a kind of inflating and stirring device of present embodiment comprises motor 1, main shaft 2, and an end of main shaft 2 links to each other by shaft coupling with the output of motor 1.At the other end of main shaft 23, four gas liquid mixture flow-guiding mouths 4 of discoid rotor are installed and evenly are provided with along the disc face of rotor 3, two rectangle air gulletings 5 that vertically are " ten " sub-shape mutually be vertically set on rotor 3 below.
Be with 8mm air gulleting below the disc-like rotor, fully the cleavage reaction still mouth of pipe of giving vent to anger overflows gas and is overflowed by the gas liquid mixture flow-guiding mouth in the running, change air flow path prolongation bubble and overflowed the time, form various circulation collisions with liquid in the reactor, improved air utilization ratio, shorten the reaction time, saved energy consumption, improved utilization rate of equipment and installations.
Claims (5)
1. inflating and stirring device, comprise motor (1), main shaft (2), one end of main shaft (2) links to each other with the output of motor (1), it is characterized in that: the other end at main shaft (2) is equipped with rotor (3), rotor (3) is provided with gas liquid mixture flow-guiding mouth (4), is provided with air gulleting (5) below the rotor (3).
2. inflating and stirring device as claimed in claim 1 is characterized in that: described rotor (3) is for discoid, and the gas liquid mixture flow-guiding mouth (4) which is provided with evenly is provided with along the disc face of rotor (3).
3. inflating and stirring device as claimed in claim 1 or 2 is characterized in that: described air gulleting (5) is a rectangle, be " ten " word shape be vertically set on rotor (3) below.
4. inflating and stirring device as claimed in claim 3 is characterized in that: the height of described air gulleting (5) is 6～10 millimeters.
5. inflating and stirring device as claimed in claim 1 or 2 is characterized in that: the diameter ratio of the diameter of described gas liquid mixture flow-guiding mouth (4) and rotor (3) is 1: 9～12.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205367599U CN201823495U (en) | 2010-09-17 | 2010-09-17 | Gas-filling stirring device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205367599U CN201823495U (en) | 2010-09-17 | 2010-09-17 | Gas-filling stirring device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201823495U true CN201823495U (en) | 2011-05-11 |
Family
ID=43962056
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205367599U Expired - Fee Related CN201823495U (en) | 2010-09-17 | 2010-09-17 | Gas-filling stirring device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201823495U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102443350A (en) * | 2011-10-17 | 2012-05-09 | 西北农林科技大学 | Ventilated raw lacquer stirrer and operating method |
| CN103240026A (en) * | 2013-05-17 | 2013-08-14 | 成都中牧生物药业有限公司 | Temperature-controlled liquid medicine granule disperser |
| CN107096434A (en) * | 2017-05-02 | 2017-08-29 | 江西省浩燃冶金设备有限责任公司 | A kind of air agitator |
| CN108584899A (en) * | 2018-08-01 | 2018-09-28 | 武汉科技大学 | A kind of porous prilled nanometer hydroxyapatite and preparation method thereof |
-
2010
- 2010-09-17 CN CN2010205367599U patent/CN201823495U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102443350A (en) * | 2011-10-17 | 2012-05-09 | 西北农林科技大学 | Ventilated raw lacquer stirrer and operating method |
| CN102443350B (en) * | 2011-10-17 | 2013-10-09 | 西北农林科技大学 | Ventilated raw lacquer stirrer |
| CN103240026A (en) * | 2013-05-17 | 2013-08-14 | 成都中牧生物药业有限公司 | Temperature-controlled liquid medicine granule disperser |
| CN107096434A (en) * | 2017-05-02 | 2017-08-29 | 江西省浩燃冶金设备有限责任公司 | A kind of air agitator |
| CN108584899A (en) * | 2018-08-01 | 2018-09-28 | 武汉科技大学 | A kind of porous prilled nanometer hydroxyapatite and preparation method thereof |
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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: 20110511 Termination date: 20160917 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |