CN2414829Y - Jet-stream whirl water and air mixer - Google Patents
Jet-stream whirl water and air mixer Download PDFInfo
- Publication number
- CN2414829Y CN2414829Y CN 00219200 CN00219200U CN2414829Y CN 2414829 Y CN2414829 Y CN 2414829Y CN 00219200 CN00219200 CN 00219200 CN 00219200 U CN00219200 U CN 00219200U CN 2414829 Y CN2414829 Y CN 2414829Y
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- water
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Abstract
The utility model relates to an injection and rotation type water and air mixer. The utility model mixes the air and the water. A water outlet end of a high-pressure water pump is orderly connected with a water injector which is provided with a breathing opening, and a spiral pipe. The high pressure water outputted by the pump is injected out in high speed by a nozzle of the water injector. Soluble air is sucked by negative pressure which is formed in the vicinity of the nozzle the breathing opening, and is carried into the water, and then the primary mixing is generated. The water and the air enter the spiral pipe with large stroke to carry out the mixing for the second time, and then the soluble air is effectively solubilized in the water in the rotation and the mixing processes. The utility model overcomes the defect that the traditional device has large volume, poor effect and high cost.
Description
The utility model relates to the jet-whirl type gas-vapor mix device that a kind of gas mixes with water.
The gas-vapor mix device is a kind of facility that the part soluble gas is dissolved in effectively water.Wherein, increasing gas-water contact area and prolongation air water incorporation time is to improve the key of dissolution velocity and dissolving quality.In order to address this problem, adopted methods such as filler bubble tower, multicell diffusion reaction pond, tower mechanical impeller, turbine injection mechanical mixer to realize usually in the past.But problems such as these methods often exist air water to mix inhomogeneous in practice operation or speed is slow, efficient is undesirable influence solute effect, and simultaneously, the conventional apparatus cost is also higher.In order to improve dissolution velocity and meltage, usually with the height that increases bubble tower, the time that prolongs the air water mixing solves.For example 1958, European Ai Erfeileide Torricelli is developed into a kind of diffusion contactor of specific type, U.S. Cleveland lifesaving appliance company developed Torricelli LMTOC experimental provision (according to international ozone association international conference paper for the third time) before 1977, obtained better effects, but above method has increased the volume of equipment greatly, brings inconvenience to practical application.
The purpose of this utility model provides a kind of soluble gas that can make fully mixes with water, and volume is small and exquisite simple, the jet-whirl type gas-vapor mix device that cost reduces significantly, and it can replace legacy equipment, is applied to relevant industry.
The purpose of this utility model is achieved in that the water side at high-pressure hydraulic pump is connected with the water sprayer and the helix tube of pneumostome successively.Water under high pressure by pump output penetrates at a high speed through the water sprayer nozzle, near the negative pressure that soluble gas forms by nozzle through pneumostome is inhaled the people and is brought in the water, enlarged gas-water contact area, produce for the first time and mix, aqueous vapor enters the helix tube of big stroke immediately, carries out the second time and mixes, and the relation that is directly proportional with pressure of the speed of utilizing gas to be dissolved in water, increased the dynamic pressure of fluid by revolving the technology of mixing, promoted the effect of mass transfer, thereby quickened the dissolving of gas.
The utility model combines owing to having adopted jet and helix tube to revolve the technology of mixing, and has obtained conspicuous effect:
1, reached the purpose that volume is little, cost is low, efficient is high.Evidence, a jet-whirl type gas-vapor mix device of per hour producing 8 tons of pure water, 0.9 ten thousand yuan of prices, the tower quasi-tradition equipment of 4.6 ten thousand yuan of equal capabilities of alternative price makes user's purchase commodity only reach 1/5 of legacy equipment, the absorption efficiency height, the ozone consumption is low.
2, in helix tube, increased the dynamic pressure of fluid, constantly changed in aqueous vapor under the situation of assembled state, improved the transfer velocity of gas, promoted mass transfer effect, gas is dissolved more fully.
3, because volume is little, in light weight, so be convenient to move and repair, simple to operate, this is to need the fixed position, set up fully outward and the legacy equipment of a series of pipelines can't be accomplished.
Concrete structure of the present utility model is provided by following embodiment and accompanying drawing:
Fig. 1 is the applicating flow chart of jet-whirl type gas-vapor mix device.
Among the figure: 1, water pump 2, water sprayer 3, helix tube 4, pressure sensitive magnetic valve 5, water inlet pipe 6, flange 7, pneumostome 8, Pressure gauge 9, outlet pipe
With reference to Fig. 1, the water pump water outlet end is connected successively with water sprayer (2), helix tube (3).Water sprayer (2) is provided with pneumostome (7).Pressure gauge (8), pressure sensitive magnetic valve (4), outlet pipe (9) are housed successively in the exit of helix tube (3).If the utility model is used for the mixing of ozone and water, when then working, start high-pressure hydraulic pump (1), water is sucked by water inlet pipe (5), enters water sprayer (2), penetrates through water sprayer inner high voltage shower nozzle, around jet, form negative pressure, and under suction function, the ozone gasification is sucked and brings into the water from pneumostome (10), produce for the first time and mix.The helix tube (3) that aqueous vapor enters big stroke immediately carries out comprehensive abundant mixing, makes ozone be dissolved in water better, has improved sterilization speed and efficient.The air water static pressure is shown by Pressure gauge (5), and sensing is controlled discharge in pressure sensitive magnetic valve (4).Air water enters output channel (8) and flows to storage tank after being passed through by pressure sensitive magnetic valve (4), and so far, the sterilization functions of ozone is also finished substantially.
Claims (3)
1, a kind of jet-whirl type gas-vapor mix device that gas is mixed with water, an end of this blender and high-pressure hydraulic pump (1) join, and it is characterized in that the water side of water pump is connected successively with water sprayer (2), helix tube (3).
2, jet-whirl type gas-vapor mix device according to claim 1 is characterized in that water sprayer (2) is provided with pneumostome (7).
3, jet-whirl type gas-vapor mix device according to claim 1 is characterized in that the exit of helix tube (3) is equipped with Pressure gauge (8), pressure sensitive magnetic valve (4), outlet pipe (9) successively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00219200 CN2414829Y (en) | 2000-01-24 | 2000-01-24 | Jet-stream whirl water and air mixer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00219200 CN2414829Y (en) | 2000-01-24 | 2000-01-24 | Jet-stream whirl water and air mixer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2414829Y true CN2414829Y (en) | 2001-01-17 |
Family
ID=33584421
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 00219200 Expired - Fee Related CN2414829Y (en) | 2000-01-24 | 2000-01-24 | Jet-stream whirl water and air mixer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2414829Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100416040C (en) * | 2003-05-29 | 2008-09-03 | 胜利石油管理局钻井工艺研究院 | Low-density fluid generator |
| CN102897911A (en) * | 2012-11-05 | 2013-01-30 | 广西金源生物化工实业有限公司 | Anaerobic tank jet-flow water distributor and water distribution blending system |
| CN103949190A (en) * | 2014-04-11 | 2014-07-30 | 浙江通源材料科技有限公司 | Industrial preparation apparatus for noble metal catalysts |
| CN104621281A (en) * | 2015-02-02 | 2015-05-20 | 江苏大学 | Intelligent oxygen dissolving method and device of oxidizing summer and autumn tea concentrated solution into instant black tea |
| CN105148714A (en) * | 2015-10-16 | 2015-12-16 | 四川大学 | Acidic waste gas treatment device |
-
2000
- 2000-01-24 CN CN 00219200 patent/CN2414829Y/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100416040C (en) * | 2003-05-29 | 2008-09-03 | 胜利石油管理局钻井工艺研究院 | Low-density fluid generator |
| CN102897911A (en) * | 2012-11-05 | 2013-01-30 | 广西金源生物化工实业有限公司 | Anaerobic tank jet-flow water distributor and water distribution blending system |
| CN102897911B (en) * | 2012-11-05 | 2014-04-02 | 广西金源生物化工实业有限公司 | Anaerobic tank jet-flow water distributor and water distribution blending system |
| CN103949190A (en) * | 2014-04-11 | 2014-07-30 | 浙江通源材料科技有限公司 | Industrial preparation apparatus for noble metal catalysts |
| CN104621281A (en) * | 2015-02-02 | 2015-05-20 | 江苏大学 | Intelligent oxygen dissolving method and device of oxidizing summer and autumn tea concentrated solution into instant black tea |
| WO2016123873A1 (en) * | 2015-02-02 | 2016-08-11 | 江苏大学 | Oxygen dissolving method and device for oxidizing summer and autumn tea concentrated solution into instant black tea |
| CN104621281B (en) * | 2015-02-02 | 2017-12-05 | 江苏大学 | A kind of intelligent oxygen dissolving method and device that Summer-autumn tea concentrate is oxidized to instant black tea |
| CN105148714A (en) * | 2015-10-16 | 2015-12-16 | 四川大学 | Acidic waste gas treatment device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |