CN206751390U - Portable chlorine dioxide gas jet device - Google Patents
Portable chlorine dioxide gas jet device Download PDFInfo
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- CN206751390U CN206751390U CN201720566755.7U CN201720566755U CN206751390U CN 206751390 U CN206751390 U CN 206751390U CN 201720566755 U CN201720566755 U CN 201720566755U CN 206751390 U CN206751390 U CN 206751390U
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- fluid reservoir
- chlorine dioxide
- stock bottle
- jet device
- dioxide gas
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Abstract
A kind of portable chlorine dioxide gas jet device, including the first stock bottle, the second stock bottle, fluid reservoir, gas tank and Venturi tube；First stock bottle is connected by the first feedstock transportation pipeline with fluid reservoir, and the second stock bottle is connected by the second feedstock transportation pipeline with fluid reservoir；Fluid reservoir is connected with gas tank, and Venturi tube is connected with fluid reservoir and gas tank.Two kinds of liquid charging stocks are delivered to fluid reservoir by the first stock bottle and the second stock bottle respectively, extraneous air enters fluid reservoir simultaneously, to reaction solution stirring and stripping chlorine dioxide, the compressed air in fluid reservoir in the chlorine dioxide and gas tank of generation enters Venturi tube, forms jet and sprays.The device makes raw material reaction thorough, avoids the harm that residual night caused by incomplete reaction brings；The structure and parameter designing of fluid reservoir cause fluid reservoir also not reveal reaction solution even if toppling over, and whole device is safe and reliable, can be manually operated, and be easy to carry operation.
Description
Technical field
It the utility model is related to a kind of chlorine dioxide for family, hotel Deng Chu lavatories or other public arena automatic disinfections
Generation and injection apparatus, belong to Chloride Dioxide Disinfection Technology field.
Background technology
It is well known that chlorine dioxide is extremely effective disinfectant, the killing ability to bacterium, virus and fungal spore
It is very strong, and will not be harmful.The preparation one of existing chlorine dioxide is to be existed using hydrochloric acid with sodium chlorate (or sodium chlorite)
Occur chemical reaction generation in the case of heating, specifically certain density sodium chlorate aqueous solution (or certain density sub- chlorine
Acid sodium aqueous solution) and certain density hydrochloric acid be quantitatively delivered in retort, generated at a certain temperature by aerated reaction
The gas-liquid mixture of chlorine dioxide and chlorine, certain density chlorine dioxide mixing thimerosal is made；Second, use sodium chlorite
Generated with citric acid reactions.
The chlorine dioxide generator equipment occurred at present is more huge, involves great expense, and quantitative conveying and multiple is needed during operation
Miscellaneous electrical control, it is not readily portable.As disclosed in Chinese patent literature CN102701156A《A kind of chlorine dioxide system
System》, disclosed in CN102502507A《The preparation facilities and its technique of chlorine dioxide》.
The content of the invention
The utility model deficiency existing for existing Chloride Dioxide Disinfection Technology, there is provided a kind of simple in construction, safety can
Lean on, be easy to carry, the portable chlorine dioxide gas jet device that can be run manually.
Portable chlorine dioxide gas jet device of the present utility model, using following technical solution：
The device, including the first stock bottle, the second stock bottle, fluid reservoir, gas tank and Venturi tube；First stock bottle passes through
First feedstock transportation pipeline is connected with fluid reservoir, and the second stock bottle is connected by the second feedstock transportation pipeline with fluid reservoir；Liquid storage
Tank is connected with gas tank, and Venturi tube is connected with fluid reservoir and gas tank.
Described device also includes first-stage reactor, and first stock bottle and the second stock bottle connect with first-stage reactor
Connect, first-stage reactor is connected with fluid reservoir.
Breather check valve is provided with first stock bottle and the second stock bottle.
Buret, conveying are disposed with the first feedstock transportation pipeline and the second feedstock transportation pipeline unidirectionally
Valve, air chamber, binder check valve, dispenser and go out liquid check valve.Buret is connected with fluid reservoir or first-stage reactor.
The fluid reservoir is connected by supply air line with gas tank, and air inlet triple valve is provided with supply air line and supply is unidirectional
Valve.
Air pump is connected with the gas tank.
The fluid reservoir is a closed tank body, and tank body internal upper part is provided with middle discharge, is provided with middle discharge
Air inlet pipe tank connected with gas, the one-level inlet pipe being connected with first-stage reactor and the chlorine dioxide discharge being connected with Venturi tube
Pipe.The one-level inlet pipe bottom extend into the bottom of fluid reservoir and is connected with aerator.
The bottom of the fluid reservoir is provided with leakage fluid dram, and tapping valve is connected with leakage fluid dram.
The fluid reservoir is square, and the inner section of fluid reservoir is in the square that the length of side is B, the internal height of fluid reservoir
H, in fluid reservoir among the external diameter of discharge be D, the height of middle discharge is h, and the volume of the first stock bottle is V1, the second original
The volume for expecting bottle is V2, then the relation of each parameter meets following formula simultaneously：
1. H=2h,
2. H=(V1+V2)/(B ﹡ (0.5B-0.52D)).
The fluid reservoir is circle, and section internal diameter be B, internal height H, and the external diameter of centre discharge is D in fluid reservoir,
The height of middle discharge is h, and the volume of the first stock bottle is V1, and the volume of the second stock bottle is V2, then each parameter relation
Meet following formula simultaneously：
1. H=2h,
2. H=(V1+V2)/((B/2-0.52D) ﹡ (B-6)/3).
The Venturi tube is connected by chlorine dioxide triple valve with fluid reservoir, and is connected by steam supply valve with gas tank.
During said apparatus concrete application, two kinds of liquid charging stocks are delivered to liquid storage by the first stock bottle and the second stock bottle respectively
Tank, while compressed air in gas tank or extraneous air enter fluid reservoir, and stripping is carried out to the chlorine dioxide generated in fluid reservoir.
The chlorine dioxide of generation is expelled directly out in certain density fluid reservoir, or enters Venturi tube by fluid reservoir, while in gas tank
Compressed air enters Venturi tube, and chlorine dioxide and compressed air mix in Venturi tube, forms jet and sprays.
The utility model is simple in construction, reacts thorough by raw material in fluid reservoir, avoids residual caused by incomplete reaction
The harm that night brings；The structure and parameter designing of fluid reservoir cause fluid reservoir also not reveal reaction solution even if toppling over, entirely
Equipment safety is reliable, can be manually operated, and be easy to carry operation.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Wherein：1. tapping valve, 2. liquid outlets, 3. fluid reservoirs, 4. aerators, 5. tracheaes, 6. middle discharges, 7. 1 is grading
Pipe, 8. first-stage reactors, 9. first burets, 10. first conveying check valves, 11. first air chambers, 12. first binder check valves,
13. the first dispenser, 14. first discharging check valves, 15. first feedstock transportation pipelines, 16. first breather check valves, 17. first
Stock bottle, 18. second titration valves, 19. second conveying check valves, 20. second air chambers, 21. second binder check valves, 22. second
Dispenser, 23. second discharging check valves, 24. second feedstock transportation pipelines, 25. second stock bottles, 26. second breather check valves,
Supplied gas check valve 27. inspection socket, 28., 29. chlorine dioxide discharge pipes, 30. discharge triple valves, 31. Venturi tubes, 32. supply
Valve, 33. safety valves, 34. gas tanks, 35. inflators, 36. air inlet triple valves, 37. supply air lines.
Embodiment
Fig. 1 gives the structure of the utility model portable chlorine dioxide gas jet device, and the device mainly includes the
One stock bottle 17, the second stock bottle 25, first-stage reactor 8, fluid reservoir 3, gas tank 34 and Venturi tube 31.On first stock bottle 17
The first breather check valve 16 is provided with, the second breather check valve 26 is provided with the second stock bottle 25.First stock bottle 17 passes through
First feedstock transportation pipeline 15 is connected with first-stage reactor 8.Second stock bottle 25 passes through the second feedstock transportation pipeline 24 and one-level
Reactor 8 connects.The first buret 9, first conveying check valve 10, the first gas are disposed with first feedstock transportation pipeline 15
Room 11, the first binder check valve 12, the first dispenser 13 and first go out liquid check valve 14, and buret 9 connects with first-stage reactor 8
Connect, first goes out liquid check valve 14 is connected with the first stock bottle 17, and the first air chamber 11 is arranged on the first conveying check valve 10 and first
Between binder check valve 12, the first dispenser 13 is arranged on first and gone out between the binder check valve 12 of liquid check valve 14 and first.The
The second buret 18, second conveying check valve 19, the second air chamber 20, the second binder are disposed with two feedstock transportation pipelines 24
Check valve 21, the second dispenser 22 and second go out liquid check valve 23, and the second buret 18 is connected with first-stage reactor 8, and second goes out
Liquid check valve 23 is connected with the second stock bottle 25, and the second air chamber 20 is arranged on the second conveying check valve 19 and the second binder check valve
Between 21, the second dispenser 22 is arranged on second and gone out between the binder check valve 21 of liquid check valve 23 and second.First dispenser 13
Syringe is used with the second dispenser 22.
The one side of first-stage reactor 8 is connected by supply air line 37 with gas tank 34, with to being exposed in first-stage reactor 8
Gas, play stirring action；On the one hand it is connected by one-level inlet pipe 7 with fluid reservoir 3, makes reaction solution continue to react into fluid reservoir 3.
Air inlet triple valve 36 and supply check valve 28 are provided with supply air line 37.Air pump 35, gas are connected with gas tank 34
Pump 35 can use manual pump.Compressed air can be pressed into gas tank 34 by air pump 35.Safety valve is provided with gas tank 34
33.Air inlet triple valve 36 to have a mouth directly and atmosphere, when starting Venturi tube 31, in fluid reservoir 3 to be formed negative
Pressure, then air can be directly sucked in by air inlet triple valve 36, and without the compressed air in gas tank 34.
Fluid reservoir 3 is a closed tank body, and its top is provided with inspection socket 27 (the used time does not block), and its internal upper part is provided with
Middle discharge 6, is provided with air inlet pipe 5, one-level inlet pipe 7 and chlorine dioxide discharge pipe 29 in middle discharge 6, air inlet pipe 5 with
Supply air line 37 connects, and its bottom stretches into the bottom of fluid reservoir 3 and is connected with aerator 4, with to being aerated in fluid reservoir 3,
The chlorine dioxide of stripping generation.Chlorine dioxide discharge pipe 29 is connected by discharging triple valve 30 with Venturi tube 31, chlorine dioxide
It can directly be discharged by discharging the floss hole of triple valve 30, floss hole can also be closed, literary mound is entered by discharge triple valve 30
In pipe 31 formed jet discharge.The bottom of fluid reservoir 3 is provided with leakage fluid dram 2, and tapping valve 1 is connected with leakage fluid dram 2.
The one side of Venturi tube 31 is connected by discharging triple valve 30 with the chlorine dioxide discharge pipe 29 of fluid reservoir 3, a side
Face is connected by steam supply valve 32 with gas tank 34, and gas tank 34 forms jet for Venturi tube 31 by steam supply valve 32 and provides source of the gas.
Liquid is not excessive during in order to ensure that fluid reservoir 3 overturns, and when fluid reservoir 3 is designed as square, its internal height is H,
The cross-sectional internal of fluid reservoir 3 is in the square that the length of side is B, and the external diameter of the middle discharge 6 of the internal upper part of fluid reservoir 3 is D, centre collection
The height of tracheae 6 is h, and the volume of the first stock bottle 17 is V1, and the volume of the second stock bottle 25 is V2, and the relation of each parameter is same
When meet following formula：
1. H=2h,
2. H=(V1+V2)/(B ﹡ (0.5B-0.52D)).
The unit of each parameter be it is unified, as B, D, h unit for centimetre when, then V1 and V2 unit is cubic centimetre.
When fluid reservoir 3 is designed as circle, a diameter of B of inner bottom surface of fluid reservoir 3, then and under the relation satisfaction of each parameter
Formula：
1. H=2h,
2. H=(V1+V2)/((B/2-0.52D) ﹡ (B-6)/3).
Using gas energy storage, actively titration is fed the utility model, can be connected by air inlet triple valve 36 with Venturi tube 31
Whether different conditions, malleation stripping process or negative pressure stripping process are realized, to realize different demands.
Two kinds of liquid charging stocks are contained in the first stock bottle 17 and the second stock bottle 25 respectively.When the first dispenser 13 (is adopted
With syringe) piston when pulling up drawing liquid, the liquid in the first stock bottle 17 goes out liquid check valve 14 by first and inhaled
Enter the first dispenser 13, air enters the first stock bottle 17 through the first breather check valve 16, balances the pressure in the first stock bottle 17
Power, when the 13 descent of piston discharge opeing of the first dispenser, first, which goes out liquid check valve 14, closes, and the first raw material is unidirectional by the first binder
Valve 12 enters air inlet chamber 11, and the gas in air chamber 11 is defeated by first again due to entrance energy storage by compression of liquid, the first raw material
Check valve 10 is sent to enter buret 9, liquid is oozed by current limliting, into first-stage reactor 8.The second raw material in second stock bottle 25
Process and the process of the first stock bottle 17 into first-stage reactor 8 are the same, are repeated no more.
Two kinds of raw materials are reacted in first-stage reactor 8, and the source of the gas provided by supply air line 37 is stirred, generation
Gas-liquid mixture pass through one-level inlet pipe 7 enter fluid reservoir 3.Extraneous air (compressed air in air or gas tank 34) warp simultaneously
The air inlet triple valve 36 and supply check valve 28 crossed on supply air line 37 enter air inlet pipe 5, the aerator 4 through the bottom of air inlet pipe 5
Spread, reaction solution is stirred and to the chlorine dioxide stripping of generation in fluid reservoir 3 in fluid reservoir 3.
The certain density chlorine dioxide of generation can be by discharge triple valve 30 by chlorine dioxide discharge pipe 29 in fluid reservoir 3
It is expelled directly out, also Venturi tube 31 can be entered by discharge triple valve 30, while the compressed air in gas tank 34 is entered through steam supply valve 32
Enter Venturi tube 31, chlorine dioxide and compressed air to mix in Venturi tube 31, form jet and spray.From gas tank 34 to liquid storage
Compressed gas is provided in tank 3, to reaction solution stirring and stripping chlorine dioxide, realizes malleation stripping process.When passing through literary mound
In pipe 31 when forming jet and spraying, negative pressure is formed in fluid reservoir 3, air can be directly sucked in by air inlet triple valve 36, to reaction solution
Stirring and stripping chlorine dioxide, realize negative pressure stripping process.
Claims (10)
1. a kind of portable chlorine dioxide gas jet device, it is characterized in that：Including the first stock bottle, the second stock bottle, liquid storage
Tank, gas tank and Venturi tube；First stock bottle is connected by the first feedstock transportation pipeline with fluid reservoir, and the second stock bottle passes through
Two feedstock transportation pipelines are connected with fluid reservoir；Fluid reservoir is connected with gas tank, and Venturi tube is connected with fluid reservoir and gas tank.
2. portable chlorine dioxide gas jet device according to claim 1, it is characterized in that：Also include first order reaction
Device, first stock bottle and the second stock bottle are connected with first-stage reactor, and first-stage reactor is connected with fluid reservoir.
3. portable chlorine dioxide gas jet device according to claim 1, it is characterized in that：First stock bottle and
Breather check valve is provided with second stock bottle.
4. portable chlorine dioxide gas jet device according to claim 1, it is characterized in that：First feedstock transportation
Buret, conveying check valve, air chamber, binder check valve, dispenser are disposed with pipeline and the second feedstock transportation pipeline
With go out liquid check valve.
5. portable chlorine dioxide gas jet device according to claim 1, it is characterized in that：The fluid reservoir passes through confession
Air pipe is connected with gas tank, and air inlet triple valve and supply check valve are provided with supply air line.
6. portable chlorine dioxide gas jet device according to claim 1, it is characterized in that：It is connected with the gas tank
Air pump.
7. portable chlorine dioxide gas jet device according to claim 1, it is characterized in that：The fluid reservoir is one close
Tank body is closed, tank body internal upper part is provided with middle discharge, and tank connected with gas air inlet pipe and one-level are provided with middle discharge
The one-level inlet pipe of reactor connection and the chlorine dioxide discharge pipe being connected with Venturi tube.
8. portable chlorine dioxide gas jet device according to claim 1, it is characterized in that：The fluid reservoir is side
Shape, in the square that the length of side is B, the internal height of fluid reservoir be H for the inner section of fluid reservoir, centre discharge in fluid reservoir
External diameter is D, and the height of middle discharge is h, and the volume of the first stock bottle is V1, and the volume of the second stock bottle is V2, then each ginseng
Several relations meets following formula simultaneously：
1. H=2h,
2. H=(V1+V2)/(B ﹡ (0.5B-0.52D)).
9. portable chlorine dioxide gas jet device according to claim 1, it is characterized in that：The fluid reservoir is circle
Shape, section internal diameter are B, internal height H, in fluid reservoir among the external diameter of discharge be D, the height of middle discharge is h, the
The volume of one stock bottle is V1, and the volume of the second stock bottle is V2, then the relation of each parameter meets following formula simultaneously：
1. H=2h,
2. H=(V1+V2)/((B/2-0.52D) ﹡ (B-6)/3).
10. portable chlorine dioxide gas jet device according to claim 1, it is characterized in that：The Venturi tube is led to
Cross chlorine dioxide triple valve to be connected with fluid reservoir, and be connected by steam supply valve with gas tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720566755.7U CN206751390U (en) | 2017-05-19 | 2017-05-19 | Portable chlorine dioxide gas jet device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720566755.7U CN206751390U (en) | 2017-05-19 | 2017-05-19 | Portable chlorine dioxide gas jet device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206751390U true CN206751390U (en) | 2017-12-15 |
Family
ID=60618888
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720566755.7U Active CN206751390U (en) | 2017-05-19 | 2017-05-19 | Portable chlorine dioxide gas jet device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206751390U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106986307A (en) * | 2017-05-19 | 2017-07-28 | 贾文敬 | Portable chlorine dioxide gas jet device |
| CN111298755A (en) * | 2020-03-18 | 2020-06-19 | 安徽敦临医疗设备有限公司 | Liquid generating device and liquid ejecting device |
-
2017
- 2017-05-19 CN CN201720566755.7U patent/CN206751390U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106986307A (en) * | 2017-05-19 | 2017-07-28 | 贾文敬 | Portable chlorine dioxide gas jet device |
| CN106986307B (en) * | 2017-05-19 | 2023-05-23 | 贾文敬 | Portable chlorine dioxide gas jet device |
| CN111298755A (en) * | 2020-03-18 | 2020-06-19 | 安徽敦临医疗设备有限公司 | Liquid generating device and liquid ejecting device |
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