CN204999609U - Gaseous chlorine dioxide's of in situ preparation sterilizing machine - Google Patents
Gaseous chlorine dioxide's of in situ preparation sterilizing machine Download PDFInfo
- Publication number
- CN204999609U CN204999609U CN201520739105.9U CN201520739105U CN204999609U CN 204999609 U CN204999609 U CN 204999609U CN 201520739105 U CN201520739105 U CN 201520739105U CN 204999609 U CN204999609 U CN 204999609U
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- reactor body
- liquid level
- sterilizing machine
- chlorine dioxide
- raw materials
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Abstract
The utility model discloses a gaseous chlorine dioxide's of in situ preparation sterilizing machine, including the reactor main part, reactor main part top is provided with the reactant import, and reactant import below is equipped with the preliminary blender of raw materials, set up aeration equipment in reactor main part lower part, set up the reaction gas export on reactor main part upper portion. The utility model discloses the technological effect of bringing is, disinfection by chlorine dioxide machine directly utilize chlorine dioxide gas to disinfect, special design through aeration equipment, air pump and measuring pump isotructure makes reactor safety, high efficiency, effectively prevents the gas leakage to furthest's assurance reactant's abundant reaction, and low in production cost can make into portable gas depoisoning machine, be applicable to the air disinfection at various occasions (for example hospital, station etc. ).
Description
Technical field
The utility model relates to a kind of disinfection by chlorine dioxide equipment, particularly relates to a kind of sterilizing machine of in situ preparation Chlorine Dioxide Gas.
Background technology
Dioxide peroxide (ClO
2) be a kind of yellow-green colour to orange-yellow gas, be known as safety, nontoxic green disinfectant in the world.The preparation method of conventional dioxide peroxide mainly contains following several: (1) sodium chlorate and concentrated hydrochloric acid reaction method (Kestiog method); (2) Textone and chlorine reaction method; (3) Potcrate and sulfurous gas reaction method; (4) Textone and hydrochloric acid reaction method; Wherein Textone and hydrochloric acid reaction method are prepare the method for high-pure chlorinedioxide, and chemical equation is: 5NaClO
2+ 4HCl=4ClO
2+ 5NaCl+2H
2o, this process products moderate purity, generally up to more than 95%, needs in situ preparation onsite application, needs the chlorine dioxide generator using high anticorrosive material to make to meet application simultaneously.
Because dioxide peroxide is soluble in water, existing disinfection by chlorine dioxide equipment is all adopt liquid dioxide peroxide to carry out disinfection, and the dioxide peroxide of liquid state carries out disinfection and not only defines the environment of its sterilization, and creates passive impact to the effect of sterilization.
Utility model content
In order to overcome above technological deficiency, the utility model provides a kind of in situ preparation chlorine dioxide gas disinfection machine, not only safely, efficiently, and may be used for the on-the-spot disinfection of various occasion.
The technical solution adopted in the utility model is as follows: a kind of sterilizing machine of in situ preparation Chlorine Dioxide Gas, comprises reactor body, and described reactor body top is provided with reaction raw materials import, is provided with the preliminary mixing tank of raw material below reaction raw materials import; Aerating apparatus is set in reactor body bottom, reaction gas outlet is set on reactor body top.
Described aerating apparatus comprises intake ducting, liquid level sealing cap and aeration plate, and the level height of the gas inlet of described intake ducting, higher than the top of reactor body, flows backwards to prevent liquid; Described aeration plate is installed on bottom reactor body, and aeration plate bottom surface is evenly provided with solarization air cap, and described aeration plate is fixedly connected with intake ducting but does not connect; Described liquid level sealing cap is installed on aeration plate, and is highly about as much as 1/3rd of reactor body; The outlet of described intake ducting extends to the top of liquid level sealing cap; First air enters the top of liquid level sealing cap by intake ducting, then the solarization air cap on aeration plate enters reactor body, impels the reaction raw materials in reactor body fully to mix;
It is individual or more that described reaction raw materials import can arrange 2-3, and install volume pump to control input speed;
Described reaction gas outlet by pipeline respectively with the top of reactor body and top mutually through, fully discharge to make the gas reflected in the preliminary mixing tank of raw material and reactor body; Described reaction gas outlet place arranges air pump, and the volume pump collaborative work of air pump and reaction raw materials ingress, controls the generation of sterilizing gas in reactor body;
Also be provided with liquid level tube bottom described reactor body, so that the liquid level of observing response device main body, be provided with residual liquid discharge valve in the bottom of liquid level tube, discharge reacted raffinate in reactor body in time.
The technique effect that the utility model brings is, chlorine dioxide disinfection machine described in the utility model directly utilizes chlorine dioxide to carry out disinfection, make reactor safely, efficiently by the isostructural particular design of aerating apparatus, air pump and volume pump, effectively prevent gas leakage, and ensure that the abundant reaction of reaction raw materials to greatest extent, and production cost is low, portable gas depoisoning machine can be made into, be applicable to the sterilizing air at various occasion (such as hospital, station etc.).
Accompanying drawing explanation
Fig. 1 is the utility model one-piece construction figure.
In figure, 1, reactor body, 2, reaction raw materials import A, 3, reaction raw materials import B, 4, the preliminary mixing tank of raw material, 5, reaction gas outlet, 6, intake ducting, 7, liquid level sealing cap, 8, aeration plate, 9, liquid level tube, 10, residual liquid discharge valve.
Embodiment
Below in conjunction with accompanying drawing and embodiment, the technical program is described in detail
A sterilizing machine in situ preparation Chlorine Dioxide Gas, comprises reactor body 1, and described reactor body 1 top is provided with reaction raw materials import, is provided with the preliminary mixing tank 4 of raw material below reaction raw materials import; Aerating apparatus is set in reactor body 1 bottom, reaction gas outlet 5 is set on reactor body 1 top.
Described aerating apparatus comprises intake ducting 6, liquid level sealing cap 7 and aeration plate 8, and the level height of the gas inlet of described intake ducting 6, higher than the top of reactor body 1, flows backwards to prevent liquid; Described aeration plate 8 is installed on bottom reactor body 1, and aeration plate 8 bottom surface is evenly provided with solarization air cap, and described aeration plate 8 is fixedly connected with intake ducting 6 but does not connect; Described liquid level sealing cap 7 is installed on aeration plate 8, and is highly about as much as 1/3rd of reactor body 1; The outlet of described intake ducting 6 extends to the top of liquid level sealing cap 7; First air enters the top of liquid level sealing cap 7 by intake ducting 6, then the solarization air cap on aeration plate 8 enters reactor body 1, impels the reaction raw materials in reactor body 1 fully to mix;
It is individual or more that described reaction raw materials import can arrange 2-3, and install volume pump to control input speed;
Described reaction gas outlet 5 by pipeline respectively with the top of reactor body 1 and top mutually through, fully discharge to make the gas reflected in the preliminary mixing tank 4 of raw material and reactor body 1; Described reaction gas outlet 5 place arranges air pump, and the volume pump collaborative work of air pump and reaction raw materials ingress, controls the generation of sterilizing gas in reactor body;
Also be provided with liquid level tube 9 bottom described reactor body 1, so that the liquid level of observing response device main body, be provided with residual liquid discharge valve 10 in the bottom of liquid level tube 9, discharge reacted raffinate in reactor body in time.
This sterilizing machine working process is, start volume pump and air pump, reaction raw materials import arranges two, is respectively reaction raw materials import A2 and reaction raw materials import B3, controlled the admission velocity of reaction raw materials by the volume pump of reaction raw materials import, reaction raw materials generally adopts Textone and hydrochloric acid; Liquid level in reactor body 1 is controlled within 1/3rd, to enable reaction fully carry out, when higher than this height, namely learns by liquid level tube 9, and discharged by residual liquid discharge valve 10; The intake ducting 6 of power aerating apparatus is provided to start to suck air by air pump, air enters into the top of liquid level sealing cap 7 by intake ducting 6, discharge at the solarization air cap on aeration plate 8, described aeration plate 8 is circular hollow structure, below homogeneous design has solarization air cap, to make the liquid level in reactor body there will not be acute variation, ensure that reaction raw materials fully reflects simultaneously; In aerating apparatus, the design of liquid level sealing cap 7 also can prevent reacting material liquid from blowing back in intake ducting 6 simultaneously, certainly has a small amount of inflow also can not have an impact to whole device;
Such dioxide peroxide produced through reaction entered reaction gas outlet and discharged, at reaction gas outlet place, can connecting hose and shower nozzle, and namely can be used for various occasion and carry out disinfection, easy and simple to handle, safety and environmental protection.
Reactor body, aeration plate and liquid level sealing cap can be designed to circle, ellipse or square according to real needs.
Easy understand; this embodiment is only a part of the present utility model; other embodiments that those skilled in the art obtain under the prerequisite not making creative work; and the various change not departing from the utility model spirit and scope carried out and modification, all should belong within protection domain of the present utility model.
Technology, shape, structure part that the utility model is not described in detail are known technology.
Claims (7)
1. a sterilizing machine in situ preparation Chlorine Dioxide Gas, is characterized in that, comprises reactor body, and described reactor body top is provided with reaction raw materials import, is provided with the preliminary mixing tank of raw material below reaction raw materials import; Aerating apparatus is set in reactor body bottom, reaction gas outlet is set on reactor body top.
2. sterilizing machine as claimed in claim 1, it is characterized in that, described aerating apparatus comprises intake ducting, liquid level sealing cap and aeration plate, and described aeration plate is installed on bottom reactor body, and aeration plate bottom surface is evenly provided with solarization air cap; Described liquid level sealing cap is installed on aeration plate; The outlet of described intake ducting extends to the top of liquid level sealing cap.
3. sterilizing machine as claimed in claim 2, is characterized in that, the level height of the gas inlet of described intake ducting is higher than the top of reactor body.
4. sterilizing machine as claimed in claim 2, it is characterized in that, the height of described liquid level sealing cap is equivalent to 1/3rd of reactor body.
5. sterilizing machine as claimed in claim 1, is characterized in that, described reaction raw materials import arranges 2-3, and is provided with volume pump to control input speed.
6. sterilizing machine as claimed in claim 1, is characterized in that, described reaction gas outlet by pipeline respectively with the top of reactor body and top mutually through; Described reaction gas outlet place arranges air pump.
7. sterilizing machine as claimed in claim 1, is characterized in that, be also provided with liquid level tube bottom described reactor body, be provided with residual liquid discharge valve in the bottom of liquid level tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520739105.9U CN204999609U (en) | 2015-09-23 | 2015-09-23 | Gaseous chlorine dioxide's of in situ preparation sterilizing machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520739105.9U CN204999609U (en) | 2015-09-23 | 2015-09-23 | Gaseous chlorine dioxide's of in situ preparation sterilizing machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204999609U true CN204999609U (en) | 2016-01-27 |
Family
ID=55156506
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520739105.9U Withdrawn - After Issue CN204999609U (en) | 2015-09-23 | 2015-09-23 | Gaseous chlorine dioxide's of in situ preparation sterilizing machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204999609U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105084317A (en) * | 2015-09-23 | 2015-11-25 | 付以坤 | Sterilizer capable of preparing gas chlorine dioxide at site |
-
2015
- 2015-09-23 CN CN201520739105.9U patent/CN204999609U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105084317A (en) * | 2015-09-23 | 2015-11-25 | 付以坤 | Sterilizer capable of preparing gas chlorine dioxide at site |
| CN105084317B (en) * | 2015-09-23 | 2018-04-10 | 付以坤 | A kind of sterilizing machine that Chlorine Dioxide Gas is prepared in situ |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160127 Effective date of abandoning: 20180410 |