CN208642344U - A kind of high-concentration ozone water manufacturing equipment for sterilizing - Google Patents
A kind of high-concentration ozone water manufacturing equipment for sterilizing Download PDFInfo
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- CN208642344U CN208642344U CN201821151887.4U CN201821151887U CN208642344U CN 208642344 U CN208642344 U CN 208642344U CN 201821151887 U CN201821151887 U CN 201821151887U CN 208642344 U CN208642344 U CN 208642344U
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- ozone water
- sterilizing
- input unit
- manufacturing equipment
- concentration ozone
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Abstract
The utility model discloses a kind of high-concentration ozone water manufacturing equipments for sterilizing, including the first input unit for storing solution and the second input unit for storing ozone, the output end of first input unit and second input unit is respectively communicated with the input terminal of low pressure vessel tank, the output end of the low pressure vessel tank is communicated with the output end of gas-liquid separated and dissolved device, the output end of the gas-liquid separated and dissolved device is connected to the liquid reserve tank for storing Ozone Water, the return pipe that Ozone Water obtained is delivered to the first supply unit is provided on the liquid reserve tank, cooling component is provided on the return pipe, the low pressure vessel tank includes liquid storage area, it is connected to the appendix of second input unit outlet end, the through-hole that multiple perforations connect the liquid storage area is offered on the appendix.The utility model at least has the following advantages: low energy consumption, the concentration for the high-concentration ozone water that can be manufactured is adjustable, to adapt to the requirement of different sterilizings.
Description
Technical field
The utility model relates to Ozone Water manufacturing equipment technical field more particularly to a kind of high concentrations for sterilizing
Ozone Water manufacturing equipment.
Background technique
Under the prior art, high-concentration ozone water be widely used in sterilizing, degradation of pesticide, water process, food fresh keeping and
The fields such as purification cleaning.At present in manufacture high-concentration ozone water, water source is generally used as using tap water, is rich in two tap water and disappears
The chlorine element of poison, it is easy to the chloroform with carcinogenic effect is formed through peroxidating.At present during use, usually
The gas-water separation of Ozone Water is carried out using high-pressure container, however high-pressure container gas-water separation effect is poor, and energy consumption is high.And it makes
The high-concentrated ozone water concentration made is relatively fixed, cannot be adjusted flexibly.
Utility model content
The technical problem to be solved by the present invention is to provide a kind of high-concentration ozone water manufactures for sterilizing to set
Standby, low energy consumption, and the concentration for the high-concentration ozone water that can be manufactured is adjustable, to adapt to the requirement of different sterilizings.
In order to solve the above-mentioned technical problem, the utility model provides a kind of high-concentration ozone water for sterilizing
Manufacturing equipment, including the first input unit for storing solution and the second input unit for storing ozone, described first
The output end of input unit and second input unit is respectively communicated with the input terminal of low pressure vessel tank, the low pressure vessel tank
Output end is communicated with the output end of gas-liquid separated and dissolved device, and the output end of the gas-liquid separated and dissolved device is connected to for storing ozone
The liquid reserve tank of water, is provided with the return pipe that Ozone Water obtained is delivered to the first supply unit on the liquid reserve tank, and described time
The cooling component for adjusting ozone coolant-temperature gage in return pipe is provided in flow tube, the low pressure vessel tank includes liquid storage area, snake
Shape is arranged in liquid storage area and is connected to by pipeline the appendix of second input unit outlet end, opens up on the appendix
There are multiple perforations to connect the through-hole of the liquid storage area.
Further, the output end of first input unit is provided with the first control group for detecting solution output quantity
Part, the output end of second input unit are provided with the second control assembly for detecting ozone output quantity.
Further, first control assembly includes first pressure regulating valve and first flowmeter；Second control
Component includes second pressure regulating valve and second flowmeter.
Further, the ratio of the first flowmeter and the second flowmeter is between 1:8.5-1:9.5.
Further, the cryogenic temperature of the cooling component is between 5-10 DEG C.
Further, third pressure-regulating valve, the number of the third pressure-regulating valve are provided in the low pressure vessel tank
Value is between 0.255-0.265Mpa.
Further, the gas-liquid separated and dissolved device is also communicated with tail gas and destroys component.
Further, it is provided with the partition extended along the vertical direction in the liquid storage area, the partition is by the liquid storage area
It is separated into the identical cavity of multiple volumes.
Further, appendix is correspondingly arranged in each cavity.
Further, the solution includes distilled water or distilled water.
By above-mentioned technical proposal, the utility model at least has the following advantages:
1, by being provided with low pressure vessel tank, low pressure vessel tank has lower energy consumption, and has preferable gas-water separation
Property；By being provided with liquid storage area and appendix, effectively ozone can be dissolved in solution, structure optimization；
2, by being provided with return pipe, high-concentration ozone water obtained can be delivered in the first input unit, is continued
It is merged with ozone, prepares the high-concentration ozone water of various concentration, to adapt to different work requirements；By being provided with cooling group
Part can effectively guarantee the temperature of high-concentration ozone water in return pipe, guarantee the higher solubility of high-concentration ozone water, function
Optimization.
Detailed description of the invention
Fig. 1 is the overall structure diagram of the utility model.
In the figures above: 1, the first input unit；2, the second input unit；3, low pressure vessel tank；4, gas-liquid separated and dissolved
Device；5, liquid reserve tank；6, return pipe；7, cooling component；8, liquid storage area；9, appendix；10, first pressure regulating valve；11, the second pressure
Force regulating valve；12, third pressure-regulating valve；13, tail gas breaking plant；14, partition.
Specific embodiment
The utility model is described in further detail in the following with reference to the drawings and specific embodiments, so that those skilled in the art
The utility model may be better understood and can be practiced, but illustrated embodiment is not as the restriction to the utility model.
As shown in connection with fig. 1, the utility model discloses a kind of manufacturing equipment of high-concentration ozone water for sterilizing,
Including the first input unit 1 for storing solution and the second input unit 2 for storing ozone, first input unit
1 and the output end of second input unit 2 be respectively communicated with the input terminal of low pressure vessel tank 3.In the utility model, preferably institute
Stating solution includes distilled water or distilled water.The output end of first input unit 1 is provided with for detecting solution output quantity
First control assembly, the output end of second input unit 2 are provided with the second control assembly for detecting ozone output quantity.
First control assembly includes first pressure regulating valve 10 and first flowmeter；Second control assembly includes second pressure
Regulating valve 11 and second flowmeter.The ratio of the first flowmeter 10 and the second flowmeter 12 1:8.5-1:9.5 it
Between.By above-mentioned set-up mode, the input quantity accounting of solution and ozone can be efficiently controlled, so that ozone be effectively ensured most
Good solubility；And be suitable for ozone and be dissolved in different types of solution, structure optimization.
The output end of the low pressure vessel tank 3 is communicated with the output end of gas-liquid separated and dissolved device, the gas-liquid separated and dissolved
The output end of device 4 is connected to the liquid reserve tank 5 for storing Ozone Water, and the low pressure vessel tank 3 exists including liquid storage area 8, snakelike setting
It is connected to the appendix 9 of 2 outlet end of the second input unit in liquid storage area 8 and by pipeline, is offered on the appendix 9 more
A perforation connects the through-hole of the liquid storage area 8.By being provided with low pressure vessel tank 3, low pressure vessel tank 3 has lower energy consumption,
And there is preferable gas-water separation；By being provided with liquid storage area 8 and appendix 9, effectively ozone can be dissolved in solution,
Structure optimization.
In the utility model, third pressure-regulating valve 12, the third pressure are provided in the preferably described low pressure vessel tank 3
The numerical value of force regulating valve 12 is between 0.255-0.265Mpa.By above-mentioned set-up mode, ozone can preferably be dissolved in steaming
In distilled water or distilled water, the generation of dissolved air water is minimized, influences the quality of Ozone Water.
The return pipe 6 that Ozone Water obtained is delivered to the first supply unit, the reflux are provided on the liquid reserve tank 5
The cooling component 7 for adjusting ozone coolant-temperature gage in return pipe 6 is provided on pipe 6.In the utility model, the preferably described cooling
The cryogenic temperature of component 7 is between 5-10 DEG C.By being provided with return pipe 6, high-concentration ozone water obtained can be delivered to
In first input unit 1, continuation is merged with ozone, prepares the high-concentration ozone water of various concentration, is needed with adapting to different work
It asks；It by being provided with cooling component 7, can effectively guarantee the temperature of high-concentration ozone water in return pipe 6, guarantee that high concentration is smelly
The higher solubility of oxygen water, function optimization.
In the utility model, the preferably described gas-liquid separated and dissolved device 4 is also communicated with tail gas and destroys component 13.Pass through setting
There is tail gas to destroy component 13, effectively the ozone not being dissolved in distilled water or distilled water can be destroyed, guarantees discharge
The safety and cleanliness of gas.
In the utility model, it is provided with the partition 14 extended along the vertical direction in the liquid storage area 8, the partition 14 is by institute
It states liquid storage area 8 and is separated into the identical cavity of multiple volumes；Appendix 9 is correspondingly arranged in each cavity.The appendix 9
Input terminal be higher than the liquid level in the liquid storage area 8, the output end of the appendix 9 is lower than the liquid in the liquid storage area 8
Face height.By above-mentioned set-up mode, it can preferably realize that ozone is dissolved in distilled water or distilled water, structure optimization.
Embodiment described above is only preferred embodiments for fully illustrating the utility model, the utility model
Protection scope it is without being limited thereto.Those skilled in the art made equivalent substitute or change on the basis of the utility model
It changes, both is within the protection scope of the present invention.The protection scope of the utility model is subject to claims.
Claims (10)
1. a kind of high-concentration ozone water manufacturing equipment for sterilizing, which is characterized in that including for storing solution
One input unit and the second input unit for storing ozone, first input unit and second input unit it is defeated
Outlet is respectively communicated with the input terminal of low pressure vessel tank, and the output end of the low pressure vessel tank is communicated with the defeated of gas-liquid separated and dissolved device
Outlet, the output end of the gas-liquid separated and dissolved device are connected to the liquid reserve tank for storing Ozone Water, are provided on the liquid reserve tank
Ozone Water obtained is delivered to the return pipe of the first supply unit, is provided on the return pipe smelly in return pipe for adjusting
The cooling component of oxygen coolant-temperature gage, the low pressure vessel tank include liquid storage area, snakelike setting in liquid storage area and by pipeline connection
The appendix of second input unit outlet end offers multiple perforations on the appendix and connects the logical of the liquid storage area
Hole.
2. being used for the high-concentration ozone water manufacturing equipment of sterilizing as described in claim 1, which is characterized in that described first
The output end of input unit is provided with the first control assembly for detecting solution output quantity, the output of second input unit
End is provided with the second control assembly for detecting ozone output quantity.
3. being used for the high-concentration ozone water manufacturing equipment of sterilizing as claimed in claim 2, which is characterized in that described first
Control assembly includes first pressure regulating valve and first flowmeter；Second control assembly includes second pressure regulating valve and
Two flowmeters.
4. being used for the high-concentration ozone water manufacturing equipment of sterilizing as claimed in claim 3, which is characterized in that described first
Flowmeter and the ratio of the second flowmeter are between 1:8.5-1:9.5.
5. being used for the high-concentration ozone water manufacturing equipment of sterilizing as described in claim 1, which is characterized in that the cooling
The cryogenic temperature of component is between 5-10 DEG C.
6. being used for the high-concentration ozone water manufacturing equipment of sterilizing as described in claim 1, which is characterized in that the low pressure
Third pressure-regulating valve is provided in container tank, the numerical value of the third pressure-regulating valve is between 0.255-0.265Mpa.
7. being used for the high-concentration ozone water manufacturing equipment of sterilizing as described in claim 1, which is characterized in that the gas-liquid
Separated and dissolved device is also communicated with tail gas and destroys component.
8. being used for the high-concentration ozone water manufacturing equipment of sterilizing as described in claim 1, which is characterized in that the liquid storage
The partition extended along the vertical direction is provided in area, the liquid storage area is separated into the identical cavity of multiple volumes by the partition.
9. being used for the high-concentration ozone water manufacturing equipment of sterilizing as claimed in claim 8, which is characterized in that each described
Appendix is correspondingly arranged in cavity.
10. being used for the high-concentration ozone water manufacturing equipment of sterilizing as described in claim 1, which is characterized in that described molten
Liquid includes distilled water or distilled water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821151887.4U CN208642344U (en) | 2018-07-19 | 2018-07-19 | A kind of high-concentration ozone water manufacturing equipment for sterilizing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821151887.4U CN208642344U (en) | 2018-07-19 | 2018-07-19 | A kind of high-concentration ozone water manufacturing equipment for sterilizing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208642344U true CN208642344U (en) | 2019-03-26 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821151887.4U Active CN208642344U (en) | 2018-07-19 | 2018-07-19 | A kind of high-concentration ozone water manufacturing equipment for sterilizing |
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| CN (1) | CN208642344U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108745013A (en) * | 2018-07-19 | 2018-11-06 | 苏州方舟环保科技有限公司 | A kind of high-concentration ozone water manufacturing equipment for sterilizing |
| TWI815010B (en) * | 2019-06-04 | 2023-09-11 | 日商荏原製作所股份有限公司 | Gas-dissolved liquid supply apparatus and gas-dissolved liquid supply method |
-
2018
- 2018-07-19 CN CN201821151887.4U patent/CN208642344U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108745013A (en) * | 2018-07-19 | 2018-11-06 | 苏州方舟环保科技有限公司 | A kind of high-concentration ozone water manufacturing equipment for sterilizing |
| CN108745013B (en) * | 2018-07-19 | 2023-11-10 | 苏州方舟环保科技有限公司 | High-concentration ozone water manufacturing equipment for sterilization and disinfection |
| TWI815010B (en) * | 2019-06-04 | 2023-09-11 | 日商荏原製作所股份有限公司 | Gas-dissolved liquid supply apparatus and gas-dissolved liquid supply method |
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