CN205999011U - A kind of gaseous chlorine dioxide generator - Google Patents
A kind of gaseous chlorine dioxide generator Download PDFInfo
- Publication number
- CN205999011U CN205999011U CN201620944951.9U CN201620944951U CN205999011U CN 205999011 U CN205999011 U CN 205999011U CN 201620944951 U CN201620944951 U CN 201620944951U CN 205999011 U CN205999011 U CN 205999011U
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- raffinate
- chlorine dioxide
- gas mixing
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Abstract
The utility model discloses a kind of gaseous chlorine dioxide generator, including primary blender, generator main body and raffinate process tank, described primary blender one end arranges charging aperture, the other end and extends in generator main body, the raffinate process tank includes one-level raffinate process tank and two grades of raffinate process tanks, the generator main body is located inside one-level raffinate process tank, is respectively provided with one-level gas mixing pipe, two grades of gas mixing pipes and three-level gas mixing pipe in the generator main body, one-level raffinate process tank and two grades of raffinate process tanks.The technique effect brought by the utility model, using fourth-order reaction, three-level gas mixing, it is sufficiently mixed raw material and initial reaction by primary blender, next enter generator main body to be reacted further and gas mixing, so that gaseous chlorine dioxide is fully discharged, then one-level raffinate process tank and two grades of raffinate process tanks are sequentially entered, carry out gas mixing reaction, by each order reaction, gas mixing, final reactivity can reach more than 90%.
Description
Technical field
The utility model is related to a kind of chlorine dioxide reaction sterilizing equipment decontaminating apparatus, and more particularly to a kind of gaseous chlorine dioxide is filled
Put.
Background technology
It is a kind of sterilized mode with disinfection by chlorine dioxide, chlorine dioxide can kill all microorganisms, including bacterium
Brood body, bacterial spore, fungi, mycobacterium and virus etc., and these bacteriums will not develop immunity to drugs.Chlorine dioxide is to micro-
Biological cell wall has stronger adsorption penetration ability, effectively can include the enzyme of sulfydryl by oxidative cell, rapidly can also suppress
The synthesis of microprotein is destroying microorganism.
Chlorine dioxide (ClO2) be a kind of yellow green to orange-yellow gas, be safe and nontoxic green disinfectant.Conventional
Chlorine dioxide preparation method mainly have following several：(1) sodium chlorate and hydrochloric acid reaction method (Kestiog method)；(2) sodium chlorate
With sulfuric acid reaction method；(3) sodium chlorite and hydrochloric acid reaction method；
Two important problems of chlorine dioxide are prepared by above-mentioned reaction, and one is how to prepare generation gaseous state titanium dioxide
Chlorine, two is exactly that reaction is thorough, makes the raffinate of discharge contain substantial amounts of acid, does not reach discharge standard, causes environmental pollution, increase
Production cost.
As chlorine dioxide is soluble in water, existing is typically all to be carried out disinfection using the chlorine dioxide of liquid, so not only
Be substantially reduced the range of disinfection by chlorine dioxide, as some large-scale place such as refuse depots etc., be not suitable for chlorine dioxide come
Sterilization；While being sterilized with liquid, effect is nothing like gaseous disinfectant, and easily causes the waste of chlorine dioxide.
Utility model content
In order to overcome above technological deficiency, the utility model provides a kind of gaseous chlorine dioxide generator, effectively solves
How reaction not thoroughly, and prepares the problem that gaseous chlorine dioxide carries out disinfection.
The technical solution adopted in the utility model is as follows：A kind of gaseous chlorine dioxide generator, including primary blender, sends out
Raw device main body and raffinate process tank, described primary blender one end arrange charging aperture, the other end and extend in generator main body, institute
Stating raffinate process tank includes one-level raffinate process tank and two grades of raffinate process tanks, and the generator main body is processed positioned at one-level raffinate
Inside tank, be respectively provided with the generator main body, one-level raffinate process tank and two grades of raffinate process tanks one-level gas mixing pipe, two grades
Gas mixing pipe and three-level gas mixing pipe.
What the utility model was brought has the technical effect that, gaseous chlorine dioxide generator described in the utility model, adopts
Fourth-order reaction, three-level gas mixing, are sufficiently mixed raw material and initial reaction by primary blender, next enter generator main body
Reacted further and gas mixing, so that gaseous chlorine dioxide is fully discharged, then sequentially enter one-level raffinate process tank and two grades residual
Liquid process tank, carries out gas mixing reaction, and by each order reaction, gas mixing, final reactivity can reach more than 90%, and raffinate is substantially
Discharged in the form of pure water, reach environmental protection discharge standard；While this product is carried out disinfection using gaseous chlorine dioxide, permissible
Suitable for large-scale places such as refuse depot, airport, hospital, station, harbour, food workshops.
Description of the drawings
It is illustrated in figure 1 the utility model overall structure figure.
In figure, 1, charging aperture A 2, charging aperture B 3, one-level raffinate process tank 4, generator main body 5, overflow gas port 6, row
Liquid mouth 7,8, two grades of gas mixing pipes 9 of one-level gas mixing pipe, heater 10, temperature control sensor 11, the second gas outlet 12, descending liquid
Pipe 13, two grades of outlets 15, three-level gas mixing pipe 16, air inlet 17 of raffinate process tank 14, raffinate, the first gas outlet 18, originals
Material partition 19, the main outlet 21 of primary blender 20, mixed liquor, mixed liquor tap 22, gas mixing hole.
Specific embodiment
Below in conjunction with the accompanying drawings 1 and specific embodiment the technical program is described in detail
A kind of gaseous chlorine dioxide generator, including primary blender 19, generator main body 4 and raffinate process tank, described
19 one end of primary blender arranges charging aperture, the other end and extends in generator main body 4, and the raffinate process tank includes that one-level is residual
Liquid process tank 3 and two grades of raffinate process tanks 13, the generator main body 4 are located inside one-level raffinate process tank 3, the generator
7, two grades of gas mixing pipes 8 and three of one-level gas mixing pipe are respectively provided with main body 4, one-level raffinate process tank 3 and two grades of raffinate process tanks 13
Level gas mixing pipe 15.
One end that the primary blender 19 arranges charging aperture is provided with the first gas outlet 17, for gas in primary blender 19
The discharge of state chlorine dioxide；The charging aperture sets at least to two, and particular number is arranged and determined with the species of reaction raw materials,
Generally two kinds raw materials, are respectively provided with charging aperture A 1 and charging aperture B 2；
Feed spacer 18 between the charging aperture by being arranged in primary blender 19 is mutually isolated, the raw material
Partition 18 extends to 19 bottom of primary blender from charging aperture, so that raw material is not produced before reaching primary blender bottom anti-
Should, excessive to prevent raw material from entering, vigorous reaction is caused, is exploded；
The part that the primary blender 19 is located in generator main body 4 is provided with the main outlet 20 of mixed liquor and mixed liquor row
Portal 21；The main outlet 20 of the mixed liquor is the angular cut positioned at 19 upper end of primary blender, the main row of the mixed liquor
The bore of outlet 20 is discharged when the main outlet 20 of mixed liquor can not meet mixed liquor less than or equal to primary 19 bore of blender
During flow, then discharged by mixed liquor tap 21, while mixed liquor tap 21 is also used for the discharge of gaseous chlorine dioxide.
4 top of the generator main body arranges the gas port 5, top that overflows and arranges leakage fluid dram 6, to discharge gaseous chlorine dioxide,
And so that mixed liquor is discharged through leakage fluid dram 6, enter one-level raffinate process tank 3；
The one-level raffinate process tank 3 arranges heater 9 and temperature control sensor 10, to control temperature in tank, makes reaction
More thorough；
The one-level raffinate process tank 3 is connected by downspout 12 with two grades of raffinate process tanks 13, the downspout 12
More than 3 centre position of one-level raffinate process tank is extended to, so that raffinate reacts more abundant in one-level raffinate process tank 3；Simultaneously
Downspout 12 is also passage of the gaseous chlorine dioxide from the two grades of entrance one-level raffinate of raffinate process tank 13 process tanks 3；
Two grades of raffinate process tanks, 13 top arranges raffinate outlet 14, and the raffinate outlet 14 connects neutralisation treatment tank,
The trace acidic in raffinate will be discharged be neutralized, so that optimum discharge standard is reached, can be discharged in the form of pure water substantially；
7, two grades of gas mixing pipes 8 of the one-level gas mixing pipe and 15 downside of three-level gas mixing pipe are respectively provided with gas mixing hole 22, three-level gas
Stir pipe and connect air inlet 16 respectively；
The second gas outlet 11 on the one-level raffinate process tank 3 is connected with the first gas outlet 17, is collected and is reflected
Chlorine dioxide carry out disinfection.
The groundwork process of this generator is that reaction raw materials such as sodium chlorate is entered by charging aperture A and charging aperture B with sulfuric acid
Primary blender 19, carries out initial reaction, subsequently into generator main body 4, in the presence of one-level gas mixing pipe 7, carries out fully
Reaction, next enters one-level raffinate process tank 3 and two grades of raffinate process tanks 13, reacts further, and the raffinate that finally discharges enters
Enter neutralizing tank, carry out acid-base neutralization.
Easy to understand, the embodiment is only a part of the present utility model, and those skilled in the art are not making wound
The property made work on the premise of the other embodiment that obtained, and carry out without departing from the various of the utility model spirit and scope
Change and modification, should all belong within protection domain of the present utility model.
Technology that the utility model is not described in detail, shape, construction part are known technology.
Claims (10)
1. a kind of gaseous chlorine dioxide generator, it is characterised in that process including primary blender, generator main body and raffinate
Tank, described primary blender one end arrange charging aperture, the other end and extend in generator main body, and the raffinate process tank includes one
Level raffinate process tank and two grades of raffinate process tanks, the generator main body are located inside one-level raffinate process tank, the generator
One-level gas mixing pipe, two grades of gas mixing pipes and three-level gas mixing is respectively provided with main body, one-level raffinate process tank and two grades of raffinate process tanks
Pipe.
2. gaseous chlorine dioxide generator as claimed in claim 1, it is characterised in that the primary blender arranges charging aperture
One end be provided with the first gas outlet, the charging aperture sets at least to two.
3. gaseous chlorine dioxide generator as claimed in claim 1, it is characterised in that by being arranged between the charging aperture
Feed spacer in primary blender is mutually isolated, and the feed spacer extends to primary blender bottom from charging aperture.
4. gaseous chlorine dioxide generator as claimed in claim 1, it is characterised in that the primary blender is located at generator
Part in main body is provided with the main outlet of mixed liquor and mixed liquor tap, the main outlet of the mixed liquor be positioned at primary mixing
The angular cut of device upper end, the bore of the main outlet of the mixed liquor is less than or equal to primary blender bore.
5. gaseous chlorine dioxide generator as claimed in claim 1, it is characterised in that the generator main body top is arranged overflows
Gas port, top arrange leakage fluid dram.
6. gaseous chlorine dioxide generator as claimed in claim 1, it is characterised in that the one-level raffinate process tank arrange plus
Thermal and temperature control sensor.
7. gaseous chlorine dioxide generator as claimed in claim 1, it is characterised in that the one-level raffinate process tank and two grades
Raffinate process tank is connected by downspout, and the downspout extends to more than one-level raffinate process tank centre position.
8. gaseous chlorine dioxide generator as claimed in claim 1, it is characterised in that two grades of raffinate process tanks top sets
Put raffinate outlet, the raffinate outlet connection neutralisation treatment tank.
9. gaseous chlorine dioxide generator as claimed in claim 1, it is characterised in that the one-level gas mixing pipe, two grades of gas mixings
Gas mixing hole is respectively provided with the downside of pipe and three-level gas mixing pipe, three-level gas mixing pipe connects air inlet respectively.
10. gaseous chlorine dioxide generator as claimed in claim 1, it is characterised in that on the one-level raffinate process tank
Second gas outlet is connected with the first gas outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620944951.9U CN205999011U (en) | 2016-08-26 | 2016-08-26 | A kind of gaseous chlorine dioxide generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620944951.9U CN205999011U (en) | 2016-08-26 | 2016-08-26 | A kind of gaseous chlorine dioxide generator |
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| Publication Number | Publication Date |
|---|---|
| CN205999011U true CN205999011U (en) | 2017-03-08 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620944951.9U Active CN205999011U (en) | 2016-08-26 | 2016-08-26 | A kind of gaseous chlorine dioxide generator |
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| Country | Link |
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| CN (1) | CN205999011U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106185820A (en) * | 2016-08-26 | 2016-12-07 | 济南科琳宝环境科技有限公司 | A kind of gaseous chlorine dioxide generator |
-
2016
- 2016-08-26 CN CN201620944951.9U patent/CN205999011U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106185820A (en) * | 2016-08-26 | 2016-12-07 | 济南科琳宝环境科技有限公司 | A kind of gaseous chlorine dioxide generator |
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| GR01 | Patent grant |