CN105084317B - A kind of sterilizing machine that Chlorine Dioxide Gas is prepared in situ - Google Patents
A kind of sterilizing machine that Chlorine Dioxide Gas is prepared in situ Download PDFInfo
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- CN105084317B CN105084317B CN201510609095.1A CN201510609095A CN105084317B CN 105084317 B CN105084317 B CN 105084317B CN 201510609095 A CN201510609095 A CN 201510609095A CN 105084317 B CN105084317 B CN 105084317B
- Authority
- CN
- China
- Prior art keywords
- reactor body
- raw materials
- reaction
- liquid level
- chlorine dioxide
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- OSVXSBDYLRYLIG-UHFFFAOYSA-N dioxidochlorine(.) Chemical compound O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 title claims abstract description 46
- 239000004155 Chlorine dioxide Substances 0.000 title claims abstract description 23
- 235000019398 chlorine dioxide Nutrition 0.000 title claims abstract description 22
- 230000001954 sterilising effect Effects 0.000 title claims abstract description 17
- 238000011065 in-situ storage Methods 0.000 title claims abstract description 9
- 239000002994 raw material Substances 0.000 claims abstract description 31
- 239000007789 gas Substances 0.000 claims abstract description 21
- 230000008676 import Effects 0.000 claims abstract description 17
- 239000012495 reaction gas Substances 0.000 claims abstract description 13
- 238000005276 aerator Methods 0.000 claims abstract description 10
- 239000007788 liquid Substances 0.000 claims description 38
- 238000005273 aeration Methods 0.000 claims description 22
- 238000007789 sealing Methods 0.000 claims description 13
- 238000004659 sterilization and disinfection Methods 0.000 abstract description 14
- 230000000694 effects Effects 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 229940099041 chlorine dioxide Drugs 0.000 description 17
- 238000000034 method Methods 0.000 description 8
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- UKLNMMHNWFDKNT-UHFFFAOYSA-M sodium chlorite Chemical compound [Na+].[O-]Cl=O UKLNMMHNWFDKNT-UHFFFAOYSA-M 0.000 description 4
- 229960002218 sodium chlorite Drugs 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- BZSXEZOLBIJVQK-UHFFFAOYSA-N 2-methylsulfonylbenzoic acid Chemical compound CS(=O)(=O)C1=CC=CC=C1C(O)=O BZSXEZOLBIJVQK-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000001154 acute effect Effects 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-ZSJDYOACSA-N heavy water Substances [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- VKJKEPKFPUWCAS-UHFFFAOYSA-M potassium chlorate Chemical compound [K+].[O-]Cl(=O)=O VKJKEPKFPUWCAS-UHFFFAOYSA-M 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
Abstract
The invention discloses a kind of sterilizing machine that Chlorine Dioxide Gas is prepared in situ, including reactor body, reaction raw materials import is provided with the top of the reactor body, the preliminary blender of raw material is provided with below reaction raw materials import；Aerator is set in reactor body bottom, reaction gas outlet is set on reactor body top.Had the technical effect that caused by the present invention, chlorine dioxide disinfection machine of the present invention is directly carried out disinfection using chlorine dioxide, it is safe efficient by aerator, air pump and the isostructural particular design reactor of measuring pump, effectively prevent gas from leaking, and the abundant reaction of reaction raw materials is ensure that to greatest extent, and production cost is low, portable gas depoisoning machine can be fabricated to, suitable for the air sterillization at various occasions (such as hospital, station etc.).
Description
Technical field
The present invention relates to a kind of disinfection by chlorine dioxide equipment, more particularly to a kind of sterilization that Chlorine Dioxide Gas is prepared in situ
Machine.
Background technology
Chlorine dioxide (ClO2) be a kind of yellow green to orange-yellow gas, be known as in the world it is safe and nontoxic green
Color disinfectant.The preparation method of conventional chlorine dioxide mainly has following several：(1) sodium chlorate and concentrated hydrochloric acid reaction method
(Kestiog methods)；(2) sodium chlorite and chlorine reaction method；(3) potassium chlorate and sulfur dioxide reaction method；(4) sodium chlorite and salt
Acid reaction method；Wherein sodium chlorite and hydrochloric acid reaction method are the method for preparing high-pure chlorinedioxide, and chemical equation is：
5NaClO2+ 4HCl=4ClO2+5NaCl+2H2O, this process products moderate purity are generally up to more than 95%, it is necessary to be prepared in situ
Field uses, while needs to disclosure satisfy that application with the chlorine dioxide generator that high anticorrosive material makes.
Existing disinfection by chlorine dioxide equipment, entered using the chlorine dioxide of liquid because chlorine dioxide is soluble in water
Row sterilization, and the chlorine dioxide of liquid carries out disinfection and not only defines the environment of its sterilization, and the effect of sterilization is generated
Negative effect.
The content of the invention
In order to overcome above technological deficiency, the present invention provides one kind and chlorine dioxide gas disinfection machine is prepared in situ, not only pacifies
Entirely, efficiently, and it can be used for the on-the-spot disinfection of various occasions.
The technical solution adopted by the present invention is as follows：A kind of sterilizing machine that Chlorine Dioxide Gas is prepared in situ, including reactor
Main body, the reactor body top are provided with reaction raw materials import, the preliminary blender of raw material are provided with below reaction raw materials import；
Aerator is set in reactor body bottom, reaction gas outlet is set on reactor body top.
The aerator includes admission line, liquid level sealing cap and aeration plate, the water of the gas access of the admission line
Flat height is higher than the top of reactor body, to prevent liquid refluence；The aeration plate is installed on reactor body bottom,
Aeration plate bottom surface is evenly arranged with solarization air cap, and the aeration plate is fixedly connected with admission line but do not connected；The liquid level envelope
Cap is installed on aeration plate, and height is about as much as 1/3rd of reactor body；The outlet extension of the admission line
To the top of liquid level sealing cap；Air initially enters the top of liquid level sealing cap by admission line, then by the aeration on aeration plate
Hole enters reactor body, promotes the reaction raw materials in reactor body to be sufficiently mixed；
The reaction raw materials import can set 2-3 or more, and install measuring pump to control charging rate；
The reaction gas outlet is mutually communicated with the top of reactor body and top respectively by pipeline, so that raw material
The gas reflected in preliminary blender and reactor body fully discharges；Air pump, gas are set at the reaction gas outlet
Pump and the measuring pump of reaction raw materials entrance cooperate, to control the generation of sterilizing gas in reactor body；
The reactor body bottom is additionally provided with liquid level tube, in order to the liquid level of observing response device main body, in liquid level
The bottom of pipe is provided with residual liquid discharge valve, discharges reacted raffinate in reactor body in time.
Had the technical effect that caused by the present invention, chlorine dioxide disinfection machine of the present invention directly utilizes chlorine dioxide
Body carries out disinfection, by aerator, air pump and the isostructural particular design reactor of measuring pump safe efficient, has
Effect prevents gas from leaking, and ensure that the abundant reaction of reaction raw materials to greatest extent, and production cost is low, can make
Into portable gas depoisoning machine, suitable for the air sterillization at various occasions (such as hospital, station etc.).
Brief description of the drawings
Fig. 1 is overall structure figure of the present invention.
In figure, 1, reactor body, 2, reaction raw materials import A, 3, reaction raw materials import B, 4, the preliminary blender of raw material, 5,
Reaction gas outlet, 6, admission line, 7, liquid level sealing cap, 8, aeration plate, 9, liquid level tube, 10, residual liquid discharge valve.
Embodiment
Below in conjunction with the accompanying drawings and the technical program is described in detail embodiment
A kind of sterilizing machine that Chlorine Dioxide Gas is prepared in situ, including reactor body 1, the top of reactor body 1
Reaction raw materials import is provided with, the preliminary blender 4 of raw material is provided with below reaction raw materials import；Set in the bottom of reactor body 1
Aerator, reaction gas outlet 5 is set on the top of reactor body 1.
The aerator includes admission line 6, liquid level sealing cap 7 and aeration plate 8, the gas access of the admission line 6
Level height be higher than reactor body 1 top, with prevent liquid refluence；The aeration plate 8 is installed on reactor master
The bottom of body 1, the bottom surface of aeration plate 8 are evenly arranged with solarization air cap, and the aeration plate 8 is fixedly connected with admission line 6 but do not connected；
The liquid level sealing cap 7 is installed on aeration plate 8, and height is about as much as 1/3rd of reactor body 1；The air inlet pipe
The outlet in road 6 extends to the top of liquid level sealing cap 7；Air initially enters the top of liquid level sealing cap 7 by admission line 6, then passes through
The solarization air cap crossed on aeration plate 8 enters reactor body 1, promotes the reaction raw materials in reactor body 1 to be sufficiently mixed；
The reaction raw materials import can set 2-3 or more, and install measuring pump to control charging rate；
The reaction gas outlet 5 is mutually communicated with the top of reactor body 1 and top respectively by pipeline, so that former
The gas for expecting to reflect in preliminary blender 4 and reactor body 1 fully discharges；Gas is set at the reaction gas outlet 5
Pump, air pump and the measuring pump of reaction raw materials entrance cooperate, to control the generation of sterilizing gas in reactor body；
The bottom of reactor body 1 is additionally provided with liquid level tube 9, in order to the liquid level of observing response device main body, in liquid
The bottom of position pipe 9 is provided with residual liquid discharge valve 10, discharges reacted raffinate in reactor body in time.
This sterilizing machine course of work is to start measuring pump and air pump, and reaction raw materials import sets two, and respectively reaction is former
Expect import A 2 and reaction raw materials import B 3, the admission velocity of reaction raw materials is controlled by the measuring pump of reaction raw materials import, instead
Raw material is answered typically to use sodium chlorite and hydrochloric acid；Liquid level in reactor body 1 is controlled within 1/3rd, so that
Reaction can be carried out fully, when higher than this height, you can learnt by liquid level tube 9, and discharged by residual liquid discharge valve 10；
The admission line 6 that power aerator is provided by air pump starts to suck air, and air enters liquid level by admission line 6 and sealed
The top of cap 7, by the solarization air cap discharge on aeration plate 8, the aeration plate 8 is circular hollow structure, lower section uniform design
There is solarization air cap, so that the liquid level in reactor body is not in acute variation, while ensure that reaction raw materials fully reflect；Aeration
The design of liquid level sealing cap 7 is also possible to prevent reacting material liquid and blowed back into admission line 6 simultaneously in device, there is a small amount of stream certainly
Entering will not also have an impact to whole device；
So entered reaction gas outlet by chlorine dioxide caused by reaction to be discharged, at reaction gas outlet,
Can be with connection flexible pipe and shower nozzle, you can carried out disinfection for various occasions, easy to operate, safety and environmental protection.
Reactor body, aeration plate and liquid level sealing cap can be designed as circular, ellipse or side according to real needs
Shape.
It is readily appreciated that, the embodiment is only the part of the present invention, and those skilled in the art are not making creativeness
The other embodiment obtained on the premise of work, and the various changes and change without departing from spirit and scope of the invention carried out
Type, it should all belong within protection scope of the present invention.
The present invention be not described in detail technology, shape, construction part be known technology.
Claims (5)
- A kind of 1. sterilizing machine that Chlorine Dioxide Gas is prepared in situ, it is characterised in that including reactor body, the reactor master Reaction raw materials import is provided with the top of body, the preliminary blender of raw material is provided with below reaction raw materials import；In reactor body bottom Aerator is set, reaction gas outlet is set on reactor body top, and the aerator includes admission line, liquid level is sealed Cap and aeration plate, the aeration plate are installed on reactor body bottom, and aeration plate bottom surface is evenly arranged with solarization air cap；The liquid level Sealing cap is installed on aeration plate, 1/3rd of height equivalent to reactor body of the liquid level sealing cap, the admission line Outlet extend to the top of liquid level sealing cap.
- 2. sterilizing machine as claimed in claim 1, it is characterised in that the level height of the gas access of the admission line is higher than The top of reactor body.
- 3. sterilizing machine as claimed in claim 1, it is characterised in that the reaction raw materials import sets 2-3, and is provided with meter Pump is measured to control charging rate.
- 4. sterilizing machine as claimed in claim 1, it is characterised in that the reaction gas outlet by pipeline respectively with reactor The top and top of main body are mutually communicated；Air pump is set at the reaction gas outlet.
- 5. sterilizing machine as claimed in claim 1, it is characterised in that the reactor body bottom is additionally provided with liquid level tube, in liquid The bottom of position pipe is provided with residual liquid discharge valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510609095.1A CN105084317B (en) | 2015-09-23 | 2015-09-23 | A kind of sterilizing machine that Chlorine Dioxide Gas is prepared in situ |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510609095.1A CN105084317B (en) | 2015-09-23 | 2015-09-23 | A kind of sterilizing machine that Chlorine Dioxide Gas is prepared in situ |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105084317A CN105084317A (en) | 2015-11-25 |
| CN105084317B true CN105084317B (en) | 2018-04-10 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510609095.1A Expired - Fee Related CN105084317B (en) | 2015-09-23 | 2015-09-23 | A kind of sterilizing machine that Chlorine Dioxide Gas is prepared in situ |
Country Status (1)
| Country | Link |
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| CN (1) | CN105084317B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106241743B (en) * | 2016-10-13 | 2018-12-25 | 济南科琳宝环境科技有限公司 | A kind of chlorine dioxide gas-liquid one reactor |
| CN112190739B (en) * | 2020-10-28 | 2024-07-23 | 晋玮璘 | Chlorine dioxide gas spraying device |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2913325Y (en) * | 2005-12-21 | 2007-06-20 | 浙江大学 | Chlorine dioxide generators |
| CN103482576A (en) * | 2013-08-23 | 2014-01-01 | 深圳欧泰华工程设备有限公司 | Method for efficiently preparing high-purity chlorine dioxide and special device thereof |
| CN103864019A (en) * | 2014-04-02 | 2014-06-18 | 山东山大华特科技股份有限公司 | Integrated chlorine dioxide preparation device and method |
| CN204999609U (en) * | 2015-09-23 | 2016-01-27 | 付以坤 | Gaseous chlorine dioxide's of in situ preparation sterilizing machine |
-
2015
- 2015-09-23 CN CN201510609095.1A patent/CN105084317B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2913325Y (en) * | 2005-12-21 | 2007-06-20 | 浙江大学 | Chlorine dioxide generators |
| CN103482576A (en) * | 2013-08-23 | 2014-01-01 | 深圳欧泰华工程设备有限公司 | Method for efficiently preparing high-purity chlorine dioxide and special device thereof |
| CN103864019A (en) * | 2014-04-02 | 2014-06-18 | 山东山大华特科技股份有限公司 | Integrated chlorine dioxide preparation device and method |
| CN204999609U (en) * | 2015-09-23 | 2016-01-27 | 付以坤 | Gaseous chlorine dioxide's of in situ preparation sterilizing machine |
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| Publication number | Publication date |
|---|---|
| CN105084317A (en) | 2015-11-25 |
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Granted publication date: 20180410 |