CN207865348U - A kind of dioxygen steam generator - Google Patents
A kind of dioxygen steam generator Download PDFInfo
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- CN207865348U CN207865348U CN201721774416.4U CN201721774416U CN207865348U CN 207865348 U CN207865348 U CN 207865348U CN 201721774416 U CN201721774416 U CN 201721774416U CN 207865348 U CN207865348 U CN 207865348U
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- fixedly installed
- bye
- pass
- compressed air
- source device
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Abstract
The utility model provides a kind of dioxygen steam generator, it is characterized in that, the dioxygen steam generator, including the second compressed air gas source device, steam unit, first compressed air gas source device, pipeline, first flow controller, second bye-pass, pressure sensor, sensor, holding vessel, suction pump, 4th bye-pass, control valve, first bye-pass, third compressed air gas source device and third bye-pass, second compressed air gas source device lower central side is fixedly installed steam unit, one end is fixedly installed the first compressed air gas source device on the right side of the steam unit lower part, one end is fixedly installed pipeline on the left of the first compressed air gas source device.The utility model simplifies hydrogen peroxide evaporation procedure so that simple in structure by the setting of steam unit, sensor, heater and pipeline；Flow control is stablized；It solves hydrogen peroxide warm and spends height, and the problem for causing decomposition rate too fast.
Description
Technical field
The utility model is related to Hydrogen Peroxide Production apparatus field, specially a kind of dioxygen steam generator.
Background technology
Using hydrogen peroxide, steam state has more the characteristics of killing bacterial spore ability than liquid condition at normal temperatures, has reached
The requirement to sterilize entirely, steam state hydrogen peroxide are 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 heats the hydrogen peroxide of mist state, so that it becomes dioxygen water vapour, to have very strong bactericidal effect.
What the compressed air that dioxygen steam generator in the prior art generally uses was generated by Venturi nozzle
Vacuum conveys hydrogen peroxide using metering pump, when using the former convey when, this mode of movement since the vacuum of generation is limited,
Suction is small, cannot be satisfied long-distance sand transport, can not also be delivered to the point of use of higher position, thus has certain limitation.
And when being conveyed using metering pump, pulse when being conveyed due to metering pump, flowed fluctuation is unstable, is also unfavorable for hydrogen peroxide
The stability contorting of concentration.
Utility model content
In order to solve the above-mentioned technical problem, the utility model provides a kind of dioxygen steam generator, existing to solve
For technology since the vacuum of generation is limited, suction is small, cannot be satisfied long-distance sand transport, has certain limitation and stability not strong
The problem of.
The utility model provides a kind of dioxygen steam generator, which is characterized in that the dioxygen steam generator,
Including the second compressed air gas source device, steam unit, the first compressed air gas source device, pipeline, first flow controller,
Two bye-passes, pressure sensor, sensor, holding vessel, suction pump, the 4th bye-pass, control valve, the first bye-pass, third pressure
Contracting air compressed air source unit and third bye-pass, the second compressed air gas source device lower central side are fixedly installed steam
Device, steam unit lower part right side one end are fixedly installed the first compressed air gas source device, first compressed air
One end is fixedly installed pipeline on the left of compressed air source unit, and pipeline left upper portion side is fixedly installed first flow controller,
First flow controller lower part side is fixedly installed the second bye-pass, and the second bye-pass Left-side center side is fixed
It is provided with pressure sensor, pressure sensor left upper portion side is fixedly installed sensor, the sensor left side one
End is fixedly installed holding vessel, and holding vessel top side is fixedly installed suction pump, suction pump upper right one end
It is fixedly installed the 4th bye-pass, one end is fixedly installed control valve, the control valve left side one on the left of the 4th bye-pass
End is fixedly installed the first bye-pass, and one end is fixedly installed third compressed air gas source device on the left of first bye-pass,
The third compressed air gas source device lower part side is fixedly installed third bye-pass.
Preferably, the steam unit, including second flow controller, atomizer and heater, the second flow
Atomizer is fixedly installed on the right side of controller lower part, having heaters is fixedly installed in atomizer lower central side.
Preferably, the sensor, including temporary storage tank and liquid level sensor, the temporary storage tank is interior to be equipped with for monitoring
The liquid level sensor of height of liquid level.
Preferably, it is connected to by third bye-pass between the second compressed air gas source device, the third bye-pass
It is equipped with the first flow controller for controlling compressed air require.
Compared with prior art, the utility model has the advantages that：Due to a kind of hydrogen peroxide of the utility model
Steam generation facility is widely used in Hydrogen Peroxide Production apparatus field.Meanwhile the beneficial effects of the utility model are：
1. the utility model simplifies hydrogen peroxide evaporation procedure so that simple in structure by the setting of steam unit.
2. the utility model, by the setting of sensor, the air pressure formed using compressed air is conveyed, its flow is made
Stablize, fed distance is remote, is used for high point.
3. the utility model is by the setting of heater, using electric heater, hydrogen peroxide is converted by liquid using electric energy
At steam state, the heating power of heater can be adjusted during heating, solved hydrogen peroxide warm and spent height, and cause decomposition rate
Too fast problem.
4. the setting that the utility model passes through pipeline so that heating speed is very fast, and dioxygen water vapour is not in heater
It stays, further reduces the decomposition of hydrogen peroxide.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model.
Fig. 2 is this utility steam apparatus structure schematic diagram.
Fig. 3 is this practicality sensor structure schematic diagram.
In figure：
Second compressed air gas source device 1, steam unit 2, second flow controller 21, atomizer 22, heater 23,
First compressed air gas source device 3, pipeline 4, first flow controller 5, the second bye-pass 6, pressure sensor 7, sensor 8,
Temporary storage tank 81, liquid level sensor 82, holding vessel 9, suction pump 10, the 4th bye-pass 11, control valve 12, the first bye-pass 13,
Three compressed air gas source devices 14, third bye-pass 15.
Specific implementation mode
The utility model is described further below in conjunction with attached drawing：
Embodiment：
As shown in attached drawing 1 to attached drawing 3
The utility model provides a kind of dioxygen steam generator, which is characterized in that the dioxygen steam generator,
Including the second compressed air gas source device 1, steam unit 2, the first compressed air gas source device 3, pipeline 4, first flow control
Device 5, the second bye-pass 6, pressure sensor 7, sensor 8, holding vessel 9, suction pump 10, the 4th bye-pass 11, control valve 12,
One bye-pass 13, third compressed air gas source device 14 and third bye-pass 15,1 lower part of the second compressed air gas source device
Center side is fixedly installed steam unit 2, and one end is fixedly installed the first compressed air gas on the right side of 2 lower part of the steam unit
Source device 3, described first compressed air gas source device, 3 left side one end are fixedly installed pipeline 4,4 left upper portion one of the pipeline
Side is fixedly installed first flow controller 5, and 5 lower part side of the first flow controller is fixedly installed the second bye-pass 6,
Second bye-pass, 6 Left-side center side is fixedly installed pressure sensor 7,7 left upper portion side of the pressure sensor
It is fixedly installed sensor 8,8 left side one end of the sensor is fixedly installed holding vessel 9, and 9 top side of the holding vessel is solid
Surely it is provided with suction pump 10,10 upper right one end of the suction pump is fixedly installed the 4th bye-pass 11, the 4th branch pipe
11 left side one end of road is fixedly installed control valve 12, and 12 left side one end of the control valve is fixedly installed the first bye-pass 13, institute
It states 13 left side one end of the first bye-pass and is fixedly installed third compressed air gas source device 14, the third compressed air gas source dress
It sets 14 lower part sides and is fixedly installed third bye-pass 15.
The steam unit 2, including second flow controller 21, atomizer 22 and heater 23, the second flow
It is fixedly installed atomizer 22 on the right side of 21 lower part of controller, 22 lower central side of the atomizer is fixedly installed heating
Device 23.
The sensor 8, including temporary storage tank 81 and liquid level sensor 82, the temporary storage tank 81 is interior to be equipped with for monitoring liquid
The liquid level sensor 82 of position height.
It is connected to by third bye-pass 15 between the second compressed air gas source device 1, on the third bye-pass 15
Equipped with the first flow controller 5 for controlling compressed air require.
Operation principle
When utility model works, the hydrogen peroxide mother liquor being stored in holding vessel 9 enters hydrogen peroxide by suction pump 10
Temporary storage tank 81 in, liquid level sensor 7 monitors the height of liquid level in hydrogen peroxide temporary storage tank 81, pressure sensor 7 in the process
The pressure in hydrogen peroxide temporary storage tank 81 is monitored, it is whether normal with monitoring situation.It is generated in first compressed air gas source device 3
Compressed air by control valve 12 also enter hydrogen peroxide temporary storage tank 81 in, so that the pressure in temporary storage tank 81 is reached the work of requirement
Make pressure.Hydrogen peroxide in temporary storage tank 81 conveys in tank under the pressure of top outward, flows through first flow controller 5 and enters mist
Change in nozzle 22.The compressed air that second compressed air gas source device 1 generates also enters atomization by second flow controller 21
In nozzle 22.Compressed air is mixed with liquid hydrogen peroxide at atomizer 22, and is entered in pipeline 4 after being atomized, in pipeline 4
Heated device 23 heats, and so that the heated vaporization of the hydrogen peroxide of liquid is become hydrogen peroxide steam and is discharged from the outlet end of main line 1.
Using technical solution described in the utility model or those skilled in the art in technical solutions of the utility model
Under inspiration, similar technical solution is designed, and reaches above-mentioned technique effect, is the protection model for falling into the utility model
It encloses.
Claims (4)
1. a kind of dioxygen steam generator, which is characterized in that the dioxygen steam generator, including the second compressed air
Compressed air source unit（1）, steam unit（2）, the first compressed air gas source device（3）, pipeline（4）, first flow controller（5）,
Two bye-passes（6）, pressure sensor（7）, sensor（8）, holding vessel（9）, suction pump（10）, the 4th bye-pass（11）, control
Valve（12）, the first bye-pass（13）, third compressed air gas source device（14）With third bye-pass（15）, the second compression sky
Gas compressed air source unit（1）Lower central side is fixedly installed steam unit（2）, the steam unit（2）One end is solid on the right side of lower part
Surely it is provided with the first compressed air gas source device（3）, the first compressed air gas source device（3）Left side one end is fixedly installed
Pipeline（4）, the pipeline（4）Left upper portion side is fixedly installed first flow controller（5）, the first flow controller
（5）Lower part side is fixedly installed the second bye-pass（6）, second bye-pass（6）Left-side center side is fixedly installed pressure
Force snesor（7）, the pressure sensor（7）Left upper portion side is fixedly installed sensor（8）, the sensor（8）It is left
Side one end is fixedly installed holding vessel（9）, the holding vessel（9）Top side is fixedly installed suction pump（10）, the suction
Pump（10）Upper right one end is fixedly installed the 4th bye-pass（11）, the 4th bye-pass（11）Left side one end is fixedly installed
There is control valve（12）, the control valve（12）Left side one end is fixedly installed the first bye-pass（13）, first bye-pass
（13）Left side one end is fixedly installed third compressed air gas source device（14）, the third compressed air gas source device（14）Under
Portion side is fixedly installed third bye-pass（15）.
2. a kind of dioxygen steam generator according to claim 1, it is characterised in that：The steam unit（2）, packet
Include second flow controller（21）, atomizer（22）And heater（23）, the second flow controller（21）On the right side of lower part
It is fixedly installed atomizer（22）, the atomizer（22）Having heaters is fixedly installed in lower central side（23）.
3. a kind of dioxygen steam generator according to claim 1, it is characterised in that：The sensor（8）, packet
Include temporary storage tank（81）And liquid level sensor（82）, the temporary storage tank（81）The interior level sensing being equipped with for monitoring height of liquid level
Device（82）.
4. a kind of dioxygen steam generator according to claim 1, it is characterised in that：The second compressed air gas
Source device（1）Between pass through third bye-pass（15）Connection, the third bye-pass（15）It is equipped with for controlling compressed air
The first flow controller of flow（5）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721774416.4U CN207865348U (en) | 2017-12-19 | 2017-12-19 | A kind of dioxygen steam generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721774416.4U CN207865348U (en) | 2017-12-19 | 2017-12-19 | A kind of dioxygen steam generator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207865348U true CN207865348U (en) | 2018-09-14 |
Family
ID=63469519
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721774416.4U Expired - Fee Related CN207865348U (en) | 2017-12-19 | 2017-12-19 | A kind of dioxygen steam generator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207865348U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114272733A (en) * | 2021-12-31 | 2022-04-05 | 山东正圣环保科技有限公司 | Hydrogen peroxide gasification catalysis increase device |
-
2017
- 2017-12-19 CN CN201721774416.4U patent/CN207865348U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114272733A (en) * | 2021-12-31 | 2022-04-05 | 山东正圣环保科技有限公司 | Hydrogen peroxide gasification catalysis increase device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180914 Termination date: 20181219 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |