CN201279443Y - Multi-level high-pressure mixing device capable of producing high-pressure ozone water - Google Patents
Multi-level high-pressure mixing device capable of producing high-pressure ozone water Download PDFInfo
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- CN201279443Y CN201279443Y CNU2008201722857U CN200820172285U CN201279443Y CN 201279443 Y CN201279443 Y CN 201279443Y CN U2008201722857 U CNU2008201722857 U CN U2008201722857U CN 200820172285 U CN200820172285 U CN 200820172285U CN 201279443 Y CN201279443 Y CN 201279443Y
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- high pressure
- pressure mixing
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- mixing bucket
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- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model discloses a multi-stage high-pressure mixing device for manufacturing high-pressure ozone water. The device is characterized in that a water inlet (1) is connected with at least two stages of high-pressure mixing buckets, and each high-pressure mixing bucket is respectively provided with a sprinkling and atomizing device, a water inlet , a water outlet and a gas inlet; a water inlet electromagnetic valve is arranged among the water inlet (1) and the high-pressure mixing buckets; a water inlet (2) is connected with the first-stage high-pressure mixing bucket, the previous-stage high-pressure mixing bucket is connected with the next-stage high-pressure mixing bucket, and the final-stage high-pressure mixing bucket is connected with a first-stage gas and water separating device (9); a high-pressure mixing bucket net rack (8-9) with a gas and water separating net (8-8) is arranged in the final-stage high-pressure mixing bucket; the first-stage gas and water separating device (9) is connected with the second-stage gas and water separating device (10), a water outlet electromagnetic valve (11), a pressure adjusting valve (12) and a water outlet (13); and the first-stage gas and water separating device (9) and a second- stage gas and water separating device (10) are connected with a gas exhaust opening (15) through a reduction device (14). The utility model has the advantages of simple structure, convenient and safe use, high mixing efficiency, long service life and low cost.
Description
Technical field:
The utility model relates to a kind of manufacturing high pressure Ozone Water, and (pressure is 0.3～7.0kg/cm
2) multistage high pressure mixing device, belong to the mixing arrangement of ozone G﹠W.
Background technology:
Ozone Water is widely used because of disinfecting and sterilizing functions is arranged, and the low pressure ozone water pressure of making is 0.15～0.25kg/cm at present
2, can't satisfy high-pressure wash and wash away the requirement that waits antiseptic hygiene to handle, and also there is the low high shortcoming of aeration rate that reaches of mixing efficiency in the mixing arrangement of low pressure Ozone Water, when ozone gas when usage space reaches certain concentration, can damage human body.If will obtain pressure is 0.3～7.0kg/cm
2The high pressure Ozone Water, then need to increase supercharging device, that supercharging device has is expensive, the shortcoming of high noisy and vibrations, and often since supercharging device can not tolerate the strong oxidation of ozone and lose efficacy in a short time.In order to solve these deficiencies, the applicant by for many years effort and a large amount of test utility model this multistage high pressure mixing device that can make the high pressure Ozone Water, can effectively improve mixing efficiency by this device, produce the Ozone Water of high pressure, make the application of Ozone Water convenient, safe, extensively.
The utility model content:
The purpose of this utility model is to overcome the deficiency of above-mentioned prior art and provides a kind of simple in structure, and is easy to use, safe, mixing efficiency height, long service life, the multistage high pressure mixing device of the manufacturing high pressure Ozone Water that cost is low.
The purpose of this utility model can realize by following measure: a kind of multistage high pressure mixing device of making the high pressure Ozone Water, it has water inlet, it is characterized in that water inlet connects two-stage high pressure mixing bucket at least respectively, every grade of high pressure mixing bucket is equipped with the inlet opening, apopore and air admission hole, be provided with entering water electromagnetic valve between the inlet opening of water inlet and high pressure mixing bucket, air inlet links to each other by the air admission hole of high-voltage tube with first order high pressure mixing bucket, the apopore of previous stage high pressure mixing bucket connects the air admission hole of next stage high pressure mixing bucket by high-voltage tube, the apopore of afterbody high pressure mixing bucket connects first order gas and water separator by high-voltage tube, every grade of high pressure mixing bucket is equipped with the spray atomising device that links to each other with the inlet opening, the inside of afterbody high pressure mixing bucket is provided with high pressure mixing bucket rack, and high pressure mixing bucket rack is provided with the gas-water separation net.The delivery port of first order gas and water separator connects the water inlet of second level gas and water separator, and the delivery port of second level gas and water separator is by going out water solenoid valve, pressure-regulating valve connection delivery port.First order gas and water separator is connected reduction apparatus with the gas outlet of second level gas and water separator, and reduction apparatus connects exhaust outlet.
In order further to realize the purpose of this utility model, described every grade of high pressure mixing bucket all has staving, the upper and lower end of staving connects high pressure mixing bucket loam cake, high pressure mixing bucket lower cover respectively, the inlet opening of high pressure mixing bucket, air admission hole are located on the high pressure mixing bucket and cover, and the apopore of high pressure mixing bucket is located under the high pressure mixing bucket and covers.
In order further to realize the purpose of this utility model, described spray atomising device connects nozzle below inlet opening, high pressure mixing bucket loam cake lower end, and nozzle connects the nozzle nut outward, and the lower end of nozzle nut inner nozzle is provided with the water spray edge of a knife.
In order further to realize the purpose of this utility model sealing between described staving and high pressure mixing bucket loam cake, the high pressure mixing bucket lower cover by the O RunddichtringO.
In order further to realize the purpose of this utility model, described high pressure mixing bucket is 2-10 grades, and promptly the quantity of high pressure mixing bucket is 2-10.
In order further to realize the purpose of this utility model, described gas-water separation net is made with ozone proof netted material.
In order further to realize the purpose of this utility model, described gas-water separation net is made with 100 orders or above micropore titanium plate net or the ozone proof netted material of 100 orders.
The utility model can produce following good effect: the utility model is 1.5～9.0kg/cm with pressure
2Running water and pressure be 0.35～9.0kg/cm
2High-pressure ozone gas carry out first order high pressure mixing, the pressure in the hybrid system is adjusted to 0.3～7.0kg/cm by water spray edge of a knife 4-7,6-7,8-7 and pressure-regulating valve 11 in every grade of tempering tank
2, after running water is carried out multistage the mixing with the mixture of ozone gas and Ozone Water.When Ozone Water is carried ozone bubbles when flowing through gas-water separation net in the afterbody tempering tank, the ozone bubbles of carrying secretly in the Ozone Water is dispersed as many microbubbles, microbubble floats, water smoke in the tempering tank is fused again to be Ozone Water with spraying into, this gas-water separation net has avoided ozone bubbles to be taken away by Ozone Water, has further improved the mixing efficiency of ozone gas and water.After passing through multistage mixing successively, also have the ozone gas of minute quantity to be mixed in the first order of flowing through in the Ozone Water and Ozone Water is separated with not water-soluble ozone gas with second level gas and water separator.The utility model adopts multistage mixing, and whole device all adopts high pressure part, high potential assembly to be formed by connecting by high-voltage tube, and can effectively produce pressure is 0.3～7.0kg/cm
2High-pressure ozone water, and the mixing efficiency of ozone gas and water is brought up to more than 80%, and be reached the effect of the ozonation aerated amount of remarkable reduction.
Description of drawings:
Fig. 1 is a structured flowchart of the present utility model;
Fig. 2 is the structural representation of multistage tempering tank of the present utility model;
Fig. 3 is the structure enlarged drawing of spray atomising device of the tempering tank of Fig. 2;
Fig. 4 is the A-A profile of Fig. 2.
The specific embodiment:
Below in conjunction with Figure of description the specific embodiment of the present utility model is elaborated:
Embodiment: a kind of multistage high pressure mixing device of making the high pressure Ozone Water is (referring to Fig. 1-Fig. 4), it has water inlet 1, water inlet 1 connects at least two high pressure mixing buckets respectively, the quantity of high pressure mixing bucket can be decided as required, the quantity of present embodiment mesohigh tempering tank is 3, it is first order high pressure mixing bucket 4, second level high pressure mixing bucket 6 and third level high pressure mixing bucket 8, water inlet 1 is connected with the inlet opening 4-1 of first order high pressure mixing bucket 4 by first order entering water electromagnetic valve 3, water inlet 1 is connected with the inlet opening 6-1 of second level high pressure mixing bucket 6 by second level entering water electromagnetic valve 5, water inlet 1 is connected with the inlet opening 8-1 of third level high pressure mixing bucket 8 by third level entering water electromagnetic valve 7, first order high pressure mixing bucket 4, the structure of second level high pressure mixing bucket 6 and third level high pressure mixing bucket 8 is basic identical, be that example illustrates its structure with high pressure mixing bucket 8 below: third level high pressure mixing bucket 8 has staving 8-10, on the staving 8-10, the lower end connects high pressure mixing bucket loam cake 8-3 by bolt 8-12 respectively, high pressure mixing bucket lower cover 8-11, and seal by O RunddichtringO 8-4.Be respectively equipped with inlet opening 8-1, air admission hole 8-2 on the end face of high pressure mixing bucket loam cake 8-3, high pressure mixing bucket lower cover 8-11 is provided with apopore 8-13.High pressure mixing bucket 8 is provided with spray atomising device (referring to Fig. 3), this device connects nozzle 8-5 below high pressure mixing bucket loam cake 8-3 lower end inlet opening 8-1, nozzle 8-5 connects nozzle nut 8-6 outward, and the lower end of nozzle nut 8-6 inner nozzle 8-5 is provided with water spray edge of a knife 8-7.The inside of afterbody high pressure mixing bucket 8 is provided with high pressure mixing bucket rack 8-9, and gas-water separation net 8-8 is installed on the rack, and gas-water separation net 8-8 makes with 100 orders or above micropore titanium plate net or other the ozone proof netted materials of 100 orders.There are not this two parts in first order high pressure mixing bucket 4 and the second level high pressure mixing bucket 6.Same first order high pressure mixing bucket 4 has staving 4-10, and the upper and lower end of staving 4-10 connects high pressure mixing bucket loam cake 4-3, high pressure mixing bucket lower cover 4-11 by bolt 4-12 respectively, and is sealed by O RunddichtringO 4-4.Be respectively equipped with inlet opening 4-1, air admission hole 4-2 on the end face of high pressure mixing bucket loam cake 4-3, high pressure mixing bucket lower cover 4-11 is provided with apopore 4-13.High pressure mixing bucket 4 is provided with the spray atomising device, and this device connects nozzle 4-5 below high pressure mixing bucket loam cake 4-3 lower end inlet opening 4-1, and nozzle 4-5 connects nozzle nut 4-6 outward, and the lower end of nozzle nut 4-6 inner nozzle 4-5 is provided with water spray edge of a knife 4-7.Second level high pressure mixing bucket 6 has staving 6-10, and the upper and lower end of staving 6-10 connects high pressure mixing bucket loam cake 6-3, high pressure mixing bucket lower cover 6-11 by bolt 6-12 respectively, and is sealed by O RunddichtringO 6-4.Be respectively equipped with inlet opening 6-1, air admission hole 6-2 on the end face of high pressure mixing bucket loam cake 6-3, high pressure mixing bucket lower cover 6-11 is provided with apopore 6-13.High pressure mixing bucket 6 is provided with the spray atomising device, and this device connects nozzle 6-5 below high pressure mixing bucket loam cake 6-3 lower end inlet opening 6-1, and nozzle 6-5 connects nozzle nut 6-6 outward, and the lower end of nozzle nut 6-6 inner nozzle 6-5 is provided with water spray edge of a knife 6-7.Air inlet 2 connects the air admission hole 4-2 of first order high pressure mixing bucket 4 by high-voltage tube, the apopore 4-13 of first order high pressure mixing bucket 4 connects the air admission hole 6-2 of second level high pressure mixing bucket 6 by high-voltage tube, the apopore 6-13 of second level high pressure mixing bucket 6 connects the air admission hole 8-2 of third level high pressure mixing bucket 8 by high-voltage tube, the apopore 8-13 of third level high pressure mixing bucket 8 connects the water inlet of first order gas and water separator 9 by high-voltage tube, the delivery port of first order gas and water separator 9 connects the water inlet of second level gas and water separator 10, and the delivery port of second level gas and water separator 10 is by going out water solenoid valve 11, pressure-regulating valve 12 connects delivery port 13.The gas outlet of the first order and second level gas and water separator is connected reduction apparatus 14, and reduction apparatus 14 connects exhaust outlet 15.
During use, open when first order entering water electromagnetic valve 3, pressure is 1.5～9.0kg/cm
2Running water enter first order tempering tank 4 from water inlet 1 through first order entering water electromagnetic valve 3, water flows into from the inlet opening 4-1 on the high pressure mixing bucket loam cake 4-3, can make current spray and effectively atomizing through the nozzle 4-5 in the nozzle nut 4-6, form very easily and the fused water smoke of ozone gas, flow is by the aperture adjustment on the water spray edge of a knife 4-7.Pressure is 0.35～9.0kg/cm
2High-pressure ozone gas enter first order tempering tank 4 through air inlet 2, ozone gas enters from the air admission hole 4-2 on the high pressure mixing bucket loam cake 4-3, meets with water smoke, air water is fused into Ozone Water, carries out the first order high pressure mixing this moment in bucket.Ozone Water and the not water-soluble ozone gas of part flow through the apopore 4-13 on the high pressure mixing bucket lower cover 4-11 together, enter second level high pressure mixing bucket 6-10 by the air admission hole 6-2 on high pressure tube connector and second the high pressure mixing bucket loam cake 6-3, second level entering water electromagnetic valve 5 is opened simultaneously, running water enters second level tempering tank 6, inlet opening 6-1 on the high pressure mixing bucket loam cake 6-3 of water from the high pressure mixing bucket 6-10 of the second level flows into, the not water-soluble ozone gas that Ozone Water is carried is carried out the second level with the water smoke of nozzle 6-5 spray atomizing and is mixed in the high pressure mixing bucket 6-10 of the second level, not water-soluble ozone gas is mixed into Ozone Water, can effectively improve mixing efficiency through the secondary high pressure mixing, but also have small amount of ozone gas not water-soluble, Ozone Water is carried small amount of ozone gas and is flow through apopore 6-13 on the high pressure mixing bucket lower cover 6-11 together, air inlet 8-2 from third level high pressure mixing bucket loam cake 8-3 flow into third level high pressure mixing bucket 8-10, third level entering water electromagnetic valve 7 is opened simultaneously, running water enters third level tempering tank 8, inlet opening 8-1 on the high pressure mixing bucket loam cake 8-3 of water from the third level high pressure mixing bucket 8-10 flows into, and carries out the third level and mix in third level high pressure mixing bucket 8-10.In the third level high pressure mixing bucket 8-10 gas-water separation net 8-8 is housed.Gas-water separation net 8-8 (referring to Fig. 4) is made by 100 orders or the micropore titanium plate net more than 100 orders or other ozone proof netted materials.When Ozone Water is carried ozone bubbles when flowing through gas-water separation net 8-8 in the third level tempering tank 8, the ozone bubbles of carrying secretly in the Ozone Water is dispersed as many microbubbles, microbubble floats, water smoke in the tempering tank is fused again to be Ozone Water with spraying into, avoided ozone bubbles to be taken away by Ozone Water, further improved the mixing efficiency of ozone G﹠W, Ozone Water is carried the apopore 8-13 that small amount of ozone gas flows through on the high pressure mixing bucket lower cover 8-11 together and is entered gas and water separator.Multistage high pressure mixing device pressure inside is to adjust to 0.3～7.0kg/cm by water spray edge of a knife 4-7,6-7,8-7 and pressure-regulating valve 11
2, to satisfy efficient demand of mixing.If the mixing efficiency of three grades of tempering tanks does not reach ideal effect, can also increase the quantity of tempering tank in addition to increase the number of times that mixes, as the 4th grade of tempering tank, the 5th grade of tempering tank ..., reach higher demand.Pass through multistage mixing successively, also have the ozone gas of minute quantity to be mixed in when flowing through first order gas and water separator 9 and second level gas and water separator 10 in the Ozone Water, Ozone Water is separated with not water-soluble ozone gas.Pressure is 0.3～7.0kg/cm
2High-pressure ozone water through going out water solenoid valve 11, pressure-regulating valve 12 flows out from delivery port 13.Ozone gas is reduced into oxygen through reduction apparatus 14 and discharges from exhaust outlet 15.
Claims (6)
1, a kind of multistage high pressure mixing device of making the high pressure Ozone Water, it has water inlet (1), it is characterized in that water inlet (1) connects two-stage high pressure mixing bucket at least respectively, every grade of high pressure mixing bucket is equipped with the inlet opening, apopore and air admission hole, be provided with entering water electromagnetic valve between the inlet opening of water inlet (1) and high pressure mixing bucket, air inlet (2) links to each other by the air admission hole of high-voltage tube with first order high pressure mixing bucket, the apopore of previous stage high pressure mixing bucket connects the air admission hole of next stage high pressure mixing bucket by high-voltage tube, the apopore of afterbody high pressure mixing bucket connects first order gas and water separator (9) by high-voltage tube, every grade of high pressure mixing bucket is equipped with the spray atomising device that links to each other with the inlet opening, the inside of afterbody high pressure mixing bucket is provided with high pressure mixing bucket rack (8-9), high pressure mixing bucket rack (8-9) is provided with gas-water separation net (8-8), the delivery port of first order gas and water separator (9) connects the water inlet of second level gas and water separator (10), and the delivery port of second level gas and water separator (10) is by going out water solenoid valve (11), pressure-regulating valve (12) connects delivery port (13).The gas outlet of first order gas and water separator (9) and second level gas and water separator (10) is connected reduction apparatus (14), and reduction apparatus (14) connects exhaust outlet (15).
2, a kind of multistage high pressure mixing device of making the high pressure Ozone Water according to claim 1, it is characterized in that described every grade of high pressure mixing bucket all has staving, the upper and lower end of staving connects high pressure mixing bucket loam cake, high pressure mixing bucket lower cover respectively, the inlet opening of high pressure mixing bucket, air admission hole are located on the high pressure mixing bucket and cover, and the apopore of high pressure mixing bucket is located under the high pressure mixing bucket and covers.
3, a kind of multistage high pressure mixing device of making the high pressure Ozone Water according to claim 1, it is characterized in that described spray atomising device connects nozzle below inlet opening, high pressure mixing bucket loam cake lower end, nozzle connects the nozzle nut outward, and the lower end of nozzle nut inner nozzle is provided with the water spray edge of a knife.
4, a kind of multistage high pressure mixing device of making the high pressure Ozone Water according to claim 2 is characterized in that being sealed by the O RunddichtringO between described staving and high pressure mixing bucket loam cake, the high pressure mixing bucket lower cover.A kind of multistage high pressure mixing device of making the high pressure Ozone Water according to claim 1 is characterized in that described high pressure mixing bucket is 2-10 grades, and promptly the quantity of high pressure mixing bucket is 2-10.
5, a kind of multistage high pressure mixing device of making the high pressure Ozone Water according to claim 1 is characterized in that described gas-water separation net makes with ozone proof netted material.
6, a kind of multistage high pressure mixing device of making the high pressure Ozone Water according to claim 6 is characterized in that described gas-water separation net (8-8) makes with 100 orders or 100 orders above micropore titanium plate net or ozone proof netted material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201722857U CN201279443Y (en) | 2008-09-22 | 2008-09-22 | Multi-level high-pressure mixing device capable of producing high-pressure ozone water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201722857U CN201279443Y (en) | 2008-09-22 | 2008-09-22 | Multi-level high-pressure mixing device capable of producing high-pressure ozone water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201279443Y true CN201279443Y (en) | 2009-07-29 |
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ID=40926331
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008201722857U Expired - Lifetime CN201279443Y (en) | 2008-09-22 | 2008-09-22 | Multi-level high-pressure mixing device capable of producing high-pressure ozone water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201279443Y (en) |
-
2008
- 2008-09-22 CN CNU2008201722857U patent/CN201279443Y/en not_active Expired - Lifetime
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20090729 Effective date of abandoning: 20080922 |