CN105402706B - A kind of dioxygen steam generator - Google Patents
A kind of dioxygen steam generator Download PDFInfo
- Publication number
- CN105402706B CN105402706B CN201510833713.0A CN201510833713A CN105402706B CN 105402706 B CN105402706 B CN 105402706B CN 201510833713 A CN201510833713 A CN 201510833713A CN 105402706 B CN105402706 B CN 105402706B
- Authority
- CN
- China
- Prior art keywords
- hydrogen peroxide
- dioxygen
- steam generator
- compressed air
- inlet
- Prior art date
- 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.)
- Active
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/28—Methods of steam generation characterised by form of heating method in boilers heated electrically
- F22B1/287—Methods of steam generation characterised by form of heating method in boilers heated electrically with water in sprays or in films
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Abstract
The invention discloses a kind of dioxygen steam generator, main line for housing mist state or steam state hydrogen peroxide, it is arranged on the atomizer of the arrival end of the main line, it is arranged on the heater on the main line, the port of export of the main line stretches out the heater, the atomizer is provided with inlet and air inlet, the dioxygen steam generator also includes the hydrogen peroxide mother liquor conveying device being connected with the inlet and the compressed air conveying device being connected with the air inlet, the hydrogen peroxide mother liquor conveying device includes the temporary storage tank for being used to store hydrogen peroxide mother liquor temporarily being connected with the inlet, the the first compressed air gas source device and hydrogen peroxide mother liquor adding set being connected respectively with the temporary storage tank.The dioxygen steam generator is simple in construction, and hydrogen peroxide is conveyed using the air pressure of compressed air formation, makes its stability of flow, and fed distance is remote, is available for high point to use.
Description
Technical field
The present invention relates to beverage production technology field, and in particular to a kind of dioxygen steam generator.
Background technology
The characteristics of gas state has more killing bacterial spore ability than liquid condition at normal temperatures using hydrogen peroxide, has reached
The requirement sterilized entirely, steam state hydrogen peroxide is usually used in the sterilizing of the confined spaces such as isolation ward, isolator.It is general in the prior art to use
Electric heater is heated to the hydrogen peroxide of mist state, so that it becomes dioxygen water vapour, so that with very strong bactericidal effect.
What the compressed air that dioxygen steam generator of the prior art is typically used was produced by Venturi nozzle
Vacuum conveys hydrogen peroxide using measuring pump, and when being conveyed using the former, this mode of movement is limited due to the vacuum of generation,
Suction is small, it is impossible to meet long-distance sand transport, can not also be delivered to the point of use of higher position, thus with certain limitation.
And when being conveyed using measuring pump, pulse when being conveyed due to measuring pump, flowed fluctuation is unstable, is also unfavorable for hydrogen peroxide
The stability contorting of concentration.
The content of the invention
The technical problems to be solved by the invention be for problem of the prior art there is provided a kind of stability of flow, conveying away from
From remote dioxygen steam generator.
To reach above-mentioned purpose, the technical solution adopted by the present invention is:
A kind of dioxygen steam generator, including for housing the main line of mist state or steam state hydrogen peroxide, being arranged on institute
The atomizer of the arrival end of main line, the heater being arranged on the main line are stated, the port of export of the main line stretches out
The heater, the atomizer is provided with inlet and air inlet, and the dioxygen steam generator also includes and institute
The hydrogen peroxide mother liquor conveying device that inlet is connected and the compressed air conveying device being connected with the air inlet are stated, it is described
Hydrogen peroxide mother liquor conveying device includes the temporary storage tank, the difference that are used to store hydrogen peroxide mother liquor temporarily being connected with the inlet
The the first compressed air gas source device and hydrogen peroxide mother liquor adding set being connected with the temporary storage tank.
Preferably, connected between the temporary storage tank and the first compressed air gas source device by the first bye-pass, institute
State the first bye-pass and be provided with the control valve for being used for controlling the pressure in the temporary storage tank.
Preferably, the liquid level sensor for being used for monitoring height of liquid level in the temporary storage tank is provided with the temporary storage tank.
Preferably, connected between the temporary storage tank and the inlet of the atomizer by the second bye-pass, institute
State the second bye-pass and be provided with the pressure sensor for being used for monitoring the temporary pressure inside the tank.
Preferably, connected between the temporary storage tank and the inlet of the atomizer by the second bye-pass, institute
State the second bye-pass and be provided with the first flow controller for being used for controlling liquid dioxygen water-carrying capacity.
Preferably, the compressed air conveying device includes the second compressed air gas source device, the institute of the atomizer
State and connected between air inlet and the second compressed air gas source device by the 3rd bye-pass, the 3rd bye-pass is provided with
Second flow controller for controlling compressed air require.
Preferably, the hydrogen peroxide mother liquor adding set includes the holding vessel for storing hydrogen peroxide mother liquor and is arranged on institute
State the suction pump on holding vessel.
Preferably, the heater uses electric heater.
Further, part of the main line in the heater is spiral shape.
Due to the utilization of above-mentioned technical proposal, the present invention has following advantages compared with prior art:The dioxygen of the present invention
Steam generator is simple in construction, and hydrogen peroxide is conveyed using the air pressure of compressed air formation, makes its stability of flow, conveys
Distance is remote, is available for high point to use.
Brief description of the drawings
Accompanying drawing 1 is the structural representation of the dioxygen steam generator of the present invention.
Embodiment
Technical scheme is further elaborated with specific embodiment below in conjunction with the accompanying drawings.
As shown in figure 1, the dioxygen steam generator of the present invention includes the master for being used to house mist state or steam state hydrogen peroxide
Pipeline 1, the atomizer 2 for being arranged on the arrival end of main line 1, the heater 3 being arranged on main line 1, the outlet of main line 1
Heater 3 is stretched out at end, and atomizer 2 is provided with inlet and air inlet, and the dioxygen steam generator also includes and feed liquor
The mouth hydrogen peroxide mother liquor conveying device being connected and the compressed air conveying device being connected with air inlet.
Hydrogen peroxide mother liquor conveying device is used for storage dioxygen jellyfish temporarily including what is be connected with the inlet of atomizer 2
The temporary storage tank 4 of liquid, the first compressed air gas source device 5 being connected respectively with temporary storage tank 4 and hydrogen peroxide mother liquor adding set.Tool
Body, hydrogen peroxide mother liquor adding set includes the holding vessel 6 for being used to store hydrogen peroxide mother liquor, leads between holding vessel 6 and temporary storage tank 4
Cross the 4th bye-pass 7 to connect, suction pump 8 is provided with the 4th bye-pass 7.First compressed air gas source device 5 and temporary storage tank 4 it
Between connected by the first bye-pass 9, connected between temporary storage tank 4 and the inlet of atomizer 2 by the second bye-pass 10.
It is provided with the first bye-pass 9 in the control valve 11 for being used for controlling pressure in temporary storage tank 4, the present embodiment, control valve
11 use pressure-reducing valve.The pressure sensor 12 and use for the pressure being respectively provided with second bye-pass 10 in monitoring temporary storage tank 4
In the first flow controller 13 of control liquid dioxygen water-carrying capacity.It is additionally provided with temporary storage tank 4 for monitoring liquid level in temporary storage tank 4
The liquid level sensor 14 of height.
Compressed air conveying device includes the second compressed air gas source device 15, the second compression control compressed air source unit 15 and mist
Connected between the air inlet for changing nozzle 2 by the 3rd bye-pass 16, second flow controller 17 be provided with the 3rd bye-pass 16,
With the flow for the compressed air for controlling to enter atomizer 2, pass through first flow controller 13 and second flow controller 16
Set, accurately control the concentration of dioxygen water vapour.
Heater 3 uses electric heater, and part of the main line 1 in heater 3 is spiral shape so that firing rate is fast.
The course of work of the dioxygen steam generator is as follows:
The hydrogen peroxide mother liquor being stored in holding vessel 6 is entered in the temporary storage tank 4 of hydrogen peroxide by suction pump 8, herein mistake
In height of liquid level in journey in the monitoring hydrogen peroxide of liquid level sensor 14 temporary storage tank 4, the monitoring hydrogen peroxide of pressure sensor 12 temporary storage tank 4
Pressure, it is whether normal with monitoring situation.The compressed air produced in first compressed air gas source device 5 passes through control valve
11 also enter in the temporary storage tank 4 of hydrogen peroxide, the pressure in temporary storage tank 4 is reached the operating pressure of requirement.Dioxygen in temporary storage tank 4
Water is outwards conveyed in tank under the pressure of top, is flowed through first flow controller 13 and is entered in atomizer 2.Second compressed air
The compressed air that compressed air source unit 15 is produced also enters in atomizer 2 by second flow controller 16.Compressed air and liquid
Hydrogen peroxide enters in main line 1 after mixing and be atomized at atomizer 4, and heated device 3 is heated in main line 1, makes liquid
The heated vaporization of hydrogen peroxide turn into hydrogen peroxide steam and discharged from the port of export of main line 1.
In summary, the hydrogen peroxide of liquid is carried out using the air pressure of compressed air formation in the dioxygen steam generator
Conveying, makes its stability of flow, and fed distance is remote, is available for high point to use.And can distinguish during hydrogen peroxide steam generation
The flow of flow and liquid hydrogen peroxide to compressed air is controlled, and the dioxygen water vapour of generation can be made to keep necessarily dense
Degree, so as to ensure bactericidal effect, while the concentration of dioxygen water vapour can pass through first flow controller and second flow controller
The middle hydrogen peroxide set respectively and the flow of compressed air are adjusted, easy to adjust.Other heater uses electric heater, profit
With electric energy by hydrogen peroxide by liquid change into steam state, heating during the heating power of heater can adjust, so as to anti-
Only hydrogen peroxide warm is spent high and causes decomposition rate too fast;The part of main line in the heater uses spiral knot simultaneously
Structure so that firing rate is very fast, and dioxygen water vapour is not stayed in heater, further reduces the decomposition of hydrogen peroxide.
The above embodiments merely illustrate the technical concept and features of the present invention, and its object is to allow person skilled in the art
Scholar can understand present disclosure and implement according to this, and it is not intended to limit the scope of the present invention.It is all according to the present invention
The equivalent change or modification that Spirit Essence is made, should all be included within the scope of the present invention.
Claims (7)
1. a kind of dioxygen steam generator, it is characterised in that:Including the main line for housing mist state or steam state hydrogen peroxide,
It is arranged on the atomizer of the arrival end of the main line, the heater being arranged on the main line, the main line goes out
The heater is stretched out at mouth end, and the atomizer is provided with inlet and air inlet, and the dioxygen steam generator is also
Conveyed including the hydrogen peroxide mother liquor conveying device being connected with the inlet and the compressed air being connected with the air inlet
Device, the hydrogen peroxide mother liquor conveying device is used for the temporary of interim storage hydrogen peroxide mother liquor including what is be connected with the inlet
The the first compressed air gas source device and hydrogen peroxide mother liquor adding set for deposit tank, being connected with the temporary storage tank respectively, it is described temporary
Deposit and connected between tank and the first compressed air gas source device by the first bye-pass, first bye-pass, which is provided with, to be used for
The control valve of the pressure in the temporary storage tank is controlled, passes through between the temporary storage tank and the inlet of the atomizer
Two bye-passes are connected, and second bye-pass is provided with the pressure sensor for being used for monitoring the temporary pressure inside the tank.
2. the dioxygen steam generator according to claim 1, it is characterised in that:Being provided with the temporary storage tank is used for
Monitor the liquid level sensor of height of liquid level in the temporary storage tank.
3. the dioxygen steam generator according to claim 1, it is characterised in that:The temporary storage tank and the atomization
Connected between the inlet of nozzle by the second bye-pass, second bye-pass, which is provided with, to be used to control liquid hydrogen peroxide
The first flow controller of flow.
4. the dioxygen steam generator according to claim 1, it is characterised in that:The compressed air conveying device
Including the second compressed air gas source device, the air inlet of the atomizer and the second compressed air gas source device it
Between by the 3rd bye-pass connect, the 3rd bye-pass be provided be used for control the second flow of compressed air require to control
Device.
5. the dioxygen steam generator according to claim 1, it is characterised in that:The hydrogen peroxide mother liquor addition dress
Put including the suction pump for storing the holding vessel of hydrogen peroxide mother liquor He being arranged on the holding vessel.
6. the dioxygen steam generator according to claim 1, it is characterised in that:The heater uses electrical heating
Device.
7. the dioxygen steam generator according to claim 1, it is characterised in that:The main line is in the heating
Part in device is spiral shape.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510833713.0A CN105402706B (en) | 2015-11-26 | 2015-11-26 | A kind of dioxygen steam generator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510833713.0A CN105402706B (en) | 2015-11-26 | 2015-11-26 | A kind of dioxygen steam generator |
Publications (2)
Publication Number | Publication Date |
---|---|
CN105402706A CN105402706A (en) | 2016-03-16 |
CN105402706B true CN105402706B (en) | 2017-10-27 |
Family
ID=55468360
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201510833713.0A Active CN105402706B (en) | 2015-11-26 | 2015-11-26 | A kind of dioxygen steam generator |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN105402706B (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107469655B (en) * | 2017-08-23 | 2021-06-25 | 江苏新美星包装机械股份有限公司 | Liquid mixing method |
CN107349876A (en) * | 2017-08-30 | 2017-11-17 | 重庆博张机电设备有限公司 | A kind of solid caustic soda production equipment and its alkali lye sugaring device |
CN109399537B (en) * | 2018-12-18 | 2023-11-21 | 南京保立隆包装机械有限公司 | Spray generating device |
CN114942301A (en) * | 2022-05-05 | 2022-08-26 | 名时(北京)科技发展有限责任公司 | Calibration system suitable for vaporized hydrogen peroxide sensor |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104986743A (en) * | 2015-07-09 | 2015-10-21 | 安徽淮化股份有限公司 | Bleaching process and device used in nitric acid preparation process |
CN105056276A (en) * | 2015-08-21 | 2015-11-18 | 江苏新美星包装机械股份有限公司 | Hydrogen peroxide sterilizing device |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2706587B1 (en) * | 1993-06-09 | 1995-11-10 | Moulinex Sa | Safety device for a boiler, in particular for an iron. |
CN202212298U (en) * | 2011-08-30 | 2012-05-09 | 广州市铭慧包装机械有限公司 | Hydrogen peroxide atomizer |
CN204477996U (en) * | 2015-02-13 | 2015-07-15 | 江苏新美星包装机械股份有限公司 | A kind of heater for the vaporization of mist state hydrogen peroxide |
CN205137401U (en) * | 2015-11-26 | 2016-04-06 | 江苏新美星包装机械股份有限公司 | Hydrogen peroxide solution steam generator |
-
2015
- 2015-11-26 CN CN201510833713.0A patent/CN105402706B/en active Active
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104986743A (en) * | 2015-07-09 | 2015-10-21 | 安徽淮化股份有限公司 | Bleaching process and device used in nitric acid preparation process |
CN105056276A (en) * | 2015-08-21 | 2015-11-18 | 江苏新美星包装机械股份有限公司 | Hydrogen peroxide sterilizing device |
Also Published As
Publication number | Publication date |
---|---|
CN105402706A (en) | 2016-03-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105402706B (en) | A kind of dioxygen steam generator | |
CN204275074U (en) | Pure vacuum sterilizer | |
CN204544876U (en) | A kind of ampoule bottle cleaning and sterilizing-drying system | |
CN203089976U (en) | Sterilizing system for filling equipment | |
JP2016125804A (en) | Humidification fan heater | |
CN207065093U (en) | A kind of vaporized hydrogen peroxide generating means | |
CN207865348U (en) | A kind of dioxygen steam generator | |
CN101825272A (en) | Preheated small-sized steam generator | |
CN106511062B (en) | Facial vaporizer with extraction function | |
CN205137401U (en) | Hydrogen peroxide solution steam generator | |
CN109399537B (en) | Spray generating device | |
CN207605717U (en) | A kind of chlorine dioxide synthetic reaction device | |
CN208703892U (en) | Electric heating assistant cleaning steam generator | |
CN204582017U (en) | A kind of normal pneumatic high-temperature steam sterilization cabinet | |
CN105584983B (en) | A kind of closed charging/discharging device and application method of volatile medium | |
CN204261083U (en) | Beverage empty bottle hydrogen peroxide vaporization sterilization device | |
CN108050500A (en) | A kind of dioxygen steam generator | |
CN102359151B (en) | Pressure-superposed water supply device | |
CN207237320U (en) | Continuous feed formula dual-effect concentrator | |
JP2014529703A (en) | Energy-saving pump and its control system | |
CN107485877A (en) | Continuous feed formula dual-effect concentrator | |
CN203018057U (en) | Ammonium nitrate solution storing and supplying device | |
CN106996553A (en) | Steam evaporator and constant temperature and humidity machine | |
MX2013001915A (en) | Machine for sterilizing the topsoil of the ground. | |
CN207175427U (en) | A kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |