CN108771987B - Manufacturing equipment for high-concentration ozone water - Google Patents
Manufacturing equipment for high-concentration ozone water Download PDFInfo
- Publication number
- CN108771987B CN108771987B CN201810798566.1A CN201810798566A CN108771987B CN 108771987 B CN108771987 B CN 108771987B CN 201810798566 A CN201810798566 A CN 201810798566A CN 108771987 B CN108771987 B CN 108771987B
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- China
- Prior art keywords
- input unit
- output end
- gas
- liquid storage
- storage area
- Prior art date
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- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 39
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 33
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 8
- 239000007788 liquid Substances 0.000 claims abstract description 45
- 238000003860 storage Methods 0.000 claims abstract description 26
- 238000004090 dissolution Methods 0.000 claims abstract description 12
- 230000005540 biological transmission Effects 0.000 claims abstract description 7
- 230000001105 regulatory effect Effects 0.000 claims description 15
- 239000012153 distilled water Substances 0.000 claims description 6
- 239000012154 double-distilled water Substances 0.000 claims description 6
- 230000006378 damage Effects 0.000 claims description 5
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 239000000243 solution Substances 0.000 description 12
- 238000005192 partition Methods 0.000 description 5
- 238000000926 separation method Methods 0.000 description 4
- 239000011550 stock solution Substances 0.000 description 3
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- 238000004659 sterilization and disinfection Methods 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01N—PRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
- A01N59/00—Biocides, pest repellants or attractants, or plant growth regulators containing elements or inorganic compounds
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Plant Pathology (AREA)
- Agronomy & Crop Science (AREA)
- Inorganic Chemistry (AREA)
- Pest Control & Pesticides (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Dentistry (AREA)
- General Health & Medical Sciences (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Environmental Sciences (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The invention discloses a manufacturing device of high-concentration ozone water, which comprises a first input unit for storing solution and a second input unit for storing ozone, wherein the output ends of the first input unit and the second input unit are respectively communicated with the input end of a low-pressure container tank, the output end of the low-pressure container tank is communicated with the output end of a gas-liquid dissolution separator, the output end of the gas-liquid dissolution separator is communicated with a liquid storage tank for storing ozone water, the output end of the first input unit is provided with a first control component for detecting the output quantity of the solution, the output end of the second input unit is provided with a second control component for detecting the output quantity of the ozone, the low-pressure container tank comprises a liquid storage area and a gas transmission pipe communicated with the output end of the second input unit through a pipeline, and the gas transmission pipe is provided with a plurality of through holes which are communicated with the liquid storage area. The invention has at least the following advantages: the energy consumption is lower, and the high-concentration ozone water with higher concentration can be prepared.
Description
Technical Field
The invention relates to the technical field of ozone water preparation, in particular to high-concentration ozone water manufacturing equipment.
Background
Under the prior art, the high-concentration ozone water is widely applied to the fields of sterilization and disinfection, pesticide degradation, water treatment, food fresh-keeping, purification and cleaning and the like. At present, tap water is generally used as a water source for preparing high-concentration ozone water, and secondary tap water is rich in chlorine elements for disinfection, so that chloroform with a carcinogenic effect is easily formed through oxidation. At present, in the using process, a high-pressure container tank is generally adopted to carry out gas-water separation of ozone water, however, the high-pressure container tank has poor gas-water separation effect and high energy consumption.
Disclosure of Invention
The invention aims to provide a manufacturing device of high-concentration ozone water, which has lower energy consumption and can prepare high-concentration ozone water with higher concentration.
In order to solve the technical problems, the invention provides high-concentration ozone water manufacturing equipment, which comprises a first input unit for storing solution and a second input unit for storing ozone, wherein the output ends of the first input unit and the second input unit are respectively communicated with the input end of a low-pressure container tank, the output end of the low-pressure container tank is communicated with the output end of a gas-liquid dissolution separator, the output end of the gas-liquid dissolution separator is communicated with a liquid storage tank for storing ozone water, the output end of the first input unit is provided with a first control component for detecting the output quantity of the solution, the output end of the second input unit is provided with a second control component for detecting the output quantity of the ozone, the low-pressure container tank comprises a liquid storage area and a gas transmission pipe which is arranged in the liquid storage area and is communicated with the output end of the second input unit through a pipeline, and a plurality of through holes which are communicated with the liquid storage area are formed in the gas transmission pipe.
Further, the first control assembly includes a first pressure regulating valve and a first flow meter; the second control assembly includes a second pressure regulating valve and a second flowmeter.
Further, the ratio of the first flow meter to the second flow meter is at 1: 8.5-1:9.5.
Further, a third pressure regulating valve is arranged in the low-pressure container tank.
Further, the value of the third regulating valve is between 0.255 and 0.265 Mpa.
Further, the gas-liquid dissolution separator is also communicated with a tail gas destruction component.
Further, a partition plate extending along the vertical direction is arranged in the liquid storage area, and the partition plate divides the liquid storage area into a plurality of cavities with the same volume.
Further, each cavity is internally provided with a gas pipe correspondingly.
Further, the input end of the air pipe is higher than the liquid level in the liquid storage area, and the output end of the air pipe is lower than the liquid level in the liquid storage area.
Further, the solution includes distilled water or double distilled water.
By means of the technical scheme, the invention has at least the following advantages:
1. by arranging the low-pressure container tank, the low-pressure container tank has lower energy consumption and better gas-water separation property; the ozone can be effectively dissolved in the solution through the arrangement of the liquid storage area and the gas transmission pipe, so that the structure is optimized;
2. the first control component and the second control component are arranged, so that the input quantity ratio of the solution to the ozone can be effectively controlled, and the optimal solubility of the ozone is effectively ensured; and can be suitable for dissolving ozone in different types of solutions, and has optimized structure.
Drawings
Fig. 1 is a schematic view of the overall structure of the present invention.
In the above figures: 1. a first input unit; 2. a second input unit; 3. a low pressure vessel; 4. a gas-liquid dissolution separator; 5. a liquid storage tank; 6. a liquid storage area; 7. a gas pipe; 8. a first pressure regulating valve; 9. a second pressure regulating valve; 10. a third pressure regulating valve; 11. a tail gas destruction assembly; 12. a partition board.
Detailed Description
The present invention will be further described with reference to the accompanying drawings and specific examples, which are not intended to be limiting, so that those skilled in the art will better understand the invention and practice it.
As shown in fig. 1, the present invention discloses a manufacturing apparatus of high concentration ozone water, comprising a first input unit 1 for storing solution and a second input unit 2 for storing ozone, wherein the output ends of the first input unit 1 and the second input unit 2 are respectively communicated with the input end of a low pressure container tank 3. In the present invention, preferably the solution comprises distilled water or double distilled water. The output end of the first input unit 1 is provided with a first control component for detecting the output quantity of the solution, and the output end of the second input unit 2 is provided with a second control component for detecting the output quantity of ozone. The first control assembly comprises a first pressure regulating valve 8 and a first flow meter; the second control assembly comprises a second pressure regulating valve 8 and a second flowmeter. The ratio of the first flow meter to the second flow meter is at 1: 8.5-1:9.5. Through the arrangement mode, the input quantity ratio of the solution and the ozone can be effectively controlled, so that the optimal solubility of the ozone is effectively ensured; and can be suitable for dissolving ozone in different types of solutions, and has optimized structure.
The output of low pressure container jar 3 is connected with the output of gas-liquid dissolution separator 4, the output intercommunication of gas-liquid dissolution separator 4 is used for storing the liquid reserve tank 5 of ozone water, low pressure container jar 3 includes stock solution district 6, snakelike setting in stock solution district 6 and through pipeline intercommunication the gas-supply pipe 7 of second input unit 2 exit end, a plurality of through-connections have been seted up on the gas-supply pipe 7 the through-hole of stock solution district 6. By arranging the low-pressure container tank 3, the low-pressure container tank 3 has lower energy consumption and better gas-water separation property; through being provided with reservoir 6 and gas-supply pipe 7, can be effectively with ozone solution, structural optimization.
In the present invention, it is preferable that the low pressure tank 3 is provided with a third pressure regulating valve 10; the value of the third regulating valve 10 is between 0.255 and 0.265 Mpa. Through the arrangement mode, ozone can be well dissolved in distilled water or double distilled water, the generation of dissolved air water is reduced as much as possible, and the quality of ozone water is affected.
In the invention, preferably, the gas-liquid dissolution separator 4 is also communicated with a tail gas destruction component 11, and by arranging the tail gas destruction component 11, ozone which is not dissolved in distilled water or double distilled water can be effectively destroyed, so that the safety and the cleanliness of the discharged gas are ensured.
In the invention, a partition plate 12 extending along the vertical direction is arranged in the liquid storage area 6, and the partition plate 12 divides the liquid storage area 6 into a plurality of cavities with the same volume. Each cavity is internally and correspondingly provided with a gas pipe 7, the input end of the gas pipe 7 is higher than the liquid level in the liquid storage area 6, and the output end of the gas pipe 7 is lower than the liquid level in the liquid storage area 6. Through the arrangement mode, ozone can be well dissolved in distilled water or double distilled water, and the structure is optimized.
The above-described embodiments are merely preferred embodiments for fully explaining the present invention, and the scope of the present invention is not limited thereto. Equivalent substitutions and modifications will occur to those skilled in the art based on the present invention, and are intended to be within the scope of the present invention. The protection scope of the invention is subject to the claims.
Claims (2)
1. The manufacturing equipment of the high-concentration ozone water is characterized by comprising a first input unit for storing solution and a second input unit for storing ozone, wherein the output ends of the first input unit and the second input unit are respectively communicated with the input end of a low-pressure container tank, the output end of the low-pressure container tank is communicated with the output end of a gas-liquid dissolution separator, the output end of the gas-liquid dissolution separator is communicated with a liquid storage tank for storing ozone water, the output end of the first input unit is provided with a first control component for detecting the output quantity of the solution, the output end of the second input unit is provided with a second control component for detecting the output quantity of the ozone, the low-pressure container tank comprises a liquid storage area and a gas transmission pipe which is arranged in the liquid storage area and is communicated with the output end of the second input unit through a pipeline, and the gas transmission pipe is provided with a plurality of through holes which are communicated with the liquid storage area; the first control assembly includes a first pressure regulating valve and a first flow meter; the second control assembly includes a second pressure regulating valve and a second flowmeter;
the ratio of the first flow meter to the second flow meter is at 1: 8.5-1:9.5;
a third pressure regulating valve is arranged in the low-pressure container tank;
the value of the third pressure regulating valve is between 0.255 and 0.265 Mpa.
2. The apparatus for producing high-concentration ozone water according to claim 1, wherein said gas-liquid dissolution separator is further connected to an exhaust gas destruction unit;
a baffle plate extending along the vertical direction is arranged in the liquid storage area, and the baffle plate divides the liquid storage area into a plurality of cavities with the same volume; a gas pipe;
the input end of the gas pipe is higher than the liquid level in the liquid storage area, and the output end of the gas pipe is lower than the liquid level in the liquid storage area, and the solution comprises distilled water or double distilled water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810798566.1A CN108771987B (en) | 2018-07-19 | 2018-07-19 | Manufacturing equipment for high-concentration ozone water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810798566.1A CN108771987B (en) | 2018-07-19 | 2018-07-19 | Manufacturing equipment for high-concentration ozone water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108771987A CN108771987A (en) | 2018-11-09 |
| CN108771987B true CN108771987B (en) | 2023-11-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810798566.1A Active CN108771987B (en) | 2018-07-19 | 2018-07-19 | Manufacturing equipment for high-concentration ozone water |
Country Status (1)
| Country | Link |
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| CN (1) | CN108771987B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111298161B (en) * | 2019-12-09 | 2021-11-16 | 河北华沃环保科技有限责任公司 | Deodorization sterilizing equipment based on ozone and odorless garbage room with same |
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| CA2775898A1 (en) * | 2009-10-02 | 2011-04-07 | Advantage Engineering Inc. | Holding tank-less water ozonating system |
| CN103100323A (en) * | 2013-02-05 | 2013-05-15 | 济南润土农业科技有限公司 | Intelligent ozone water preparing system |
| CN203451272U (en) * | 2013-08-22 | 2014-02-26 | 广东鼎湖山泉有限公司 | Ozone addition device |
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| CN108771987A (en) | 2018-11-09 |
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