CN105854718A - Improved hydrogen peroxide mixing bubbling system - Google Patents
Improved hydrogen peroxide mixing bubbling system Download PDFInfo
- Publication number
- CN105854718A CN105854718A CN201510026370.7A CN201510026370A CN105854718A CN 105854718 A CN105854718 A CN 105854718A CN 201510026370 A CN201510026370 A CN 201510026370A CN 105854718 A CN105854718 A CN 105854718A
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- Prior art keywords
- venthole
- hydrogen peroxide
- container
- defecator
- modified model
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Abstract
The invention relates to an improved hydrogen peroxide mixing bubbling system. The system comprises a gas source, a filtering apparatus, an air inlet pipe and a container, hydrogen peroxide is arranged in a container, the air inlet pipe is stretched into the container, the other end is connected with the gas source through the filtering apparatus, the air inlet pipe is in a L-shaped structure and is vertically stretched into the bottom of the container and is transversely laid on the bottom of the container, an end part of the air inlet pipe is sealed, and several air outlets are arranged on the pipe body. Compared with the prior art, the hydrogen peroxide in the container is uniformly mixed, and the system has the advantages of high operating efficiency and convenient operation.
Description
Technical field
The present invention relates to a kind of bubble systems, especially relate to a kind of modified model hydrogen peroxide mixing bubble systems.
Background technology
Need sufficiently to mix before particular stage hydrogen peroxide is packed, ensure that the concentration of various piece in trough is the most equal
One, the method that we used in the past is: beat circulation, a 60m with pump3If storage tank 15m3/ h's
There is certain restriction the 8 hours pump mix homogeneously minimum time (volume mixture of 2 times) because of the power of pump, so
The hydrogen peroxide generally mixing with what a groove tank needs the substantial amounts of time, and is not fee from the dead angle inside groove tank, with
Shi Yinwei pump and groove tank are taken for a long time, it is impossible to charging produces and packaging, limits the production capacity of particular stage hydrogen peroxide.
Chinese patent CN103962037A discloses a kind of for the well-mixed bubble systems of hydrogen peroxide, including
Source of the gas, defecator, bubbling pipe and container, hydrogen peroxide is located in container, in bubbling pipe outlet submergence hydrogen peroxide,
Import is connected with source of the gas by defecator, although there is the problem at dead angle in this system in can solve the problem that groove tank, but
Owing to its bubbling pipe being passed in container is to arrange from top to bottom, and it is suspended in the middle of container, causes it to cannot
It is applied to the hydrogen peroxide of upper strata and lower floor, is merely able to the hydrogen peroxide near line up and carries out bubbling mixing, cause container
Interior hydrogen peroxide mixing is uneven, it is impossible to realize efficiently distribution.
Summary of the invention
Defect that the purpose of the present invention is contemplated to overcome above-mentioned prior art to exist and in providing one to make container
The modified model hydrogen peroxide mixing bubble systems that the mixing of hydrogen peroxide is more uniform, work efficiency is higher, easy to operate.
The purpose of the present invention can be achieved through the following technical solutions:
A kind of modified model hydrogen peroxide mixing bubble systems, including source of the gas, defecator, air inlet pipe and container, described
Hydrogen peroxide be located in container, described air inlet pipe extend in container, and the other end is connected with source of the gas through defecator,
Described air inlet pipe is L-shaped structure, vertically extend into the bottom of container, is laterally laid on container bottoms, enters
The end seal of trachea, pipe shaft is provided with multiple venthole.
It is laid in the transverse pipe on container bottoms the branched pipe being also associated with several perpendicular setting, this branched pipe
On be provided with venthole.
Preferably, vertical duct in difference towards on be equipped with venthole, the venthole aperture of top is less, respectively goes out
Spacing between pore is relatively big, and the venthole aperture of lower section is relatively big, and the spacing between each venthole is less.
It is further preferred that the aperture of the venthole of top is 2mm, the spacing between each venthole is 10cm.
It is further preferred that the aperture of the venthole of lower section is 3mm, the spacing between each venthole is 5cm.
It is further preferred that the venthole with transverse pipe is 45 ° of direction perforates obliquely, the aperture of venthole is
3mm, the spacing between each venthole is 5cm.
It is further preferred that the venthole on branched pipe is 45 ° of direction perforates obliquely, the aperture of venthole is
2mm, the spacing between each venthole is 10cm.
Preferably, it is connected between source of the gas with defecator to have and prevents moisture in gas phase from entering the dew point monitoring in hydrogen peroxide
Device.
Preferably, the pipeline that defecator is connected with container is provided with interval bubbling and controls valve and pressure alarm dress
Put.
Preferably, defecator is also associated with Backwash pipeline, the two ends of this pipeline respectively with defecator and mistake
Pipeline between filter device and container is connected, and arranges back flush valves in Backwash pipeline.
Preferably, defecator is particle filtering unit, drying unit and the activated carbon adsorption unit being sequentially connected with
Three-level filter device, particle filtering unit is multiple stage filter units, may filter that the granule of more than diameter 0.01 μm,
Follow-up drying unit and activated carbon adsorption unit remove moisture in air further, it is ensured that the degree of purity of hydrogen peroxide,
Avoid introducing impurity effect degree of purity, and the pressure of more convenient control bubbling in hydrogen peroxide product.
Compared with prior art, the invention have the advantages that
1, by improving air inlet pipe, by adjusting the distributed controll hydrogen peroxide of the perforate of the pore stream when mixing
To, the performance of improvement local turbulence is to improve mixed performance, additionally by the blowing angle and the arrangement that adjust pore
Substantially increase the efficiency of batch mixing so that in container, the mixing of hydrogen peroxide is more uniform；
2, improve work efficiency, a 60m3Groove tank has only to 15-20 minutes and just can be sufficiently mixed, logical
Cross different time points sample analysis and obtained good effect, the time of 80% can be saved, and in ensure that groove tank
Being sufficiently mixed of material；
3, easy to operate, reliability is high, in three-level filter device, utilizes particle filtering unit to filter out diameter
Granule more than 0.01 μm, follow-up drying unit and activated carbon adsorption unit remove further moisture in air,
Mist of oils etc. enter the pressure that simultaneously can effectively control bubbling in finished product hydrogen peroxide, it is to avoid compressed-air actuated waste.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
In figure, 1-source of the gas, 2-dew point supervising device, 3-defecator, 4-back flush valves, 5-pressure alarm fill
Put, 6-gap bubbling controls valve, 7-container, 8-air inlet pipe, the vertical pipe shaft of 81-, the horizontal pipe shaft of 82-, 83-divide
Arm, 9-venthole.
Detailed description of the invention
The present invention is described in detail with specific embodiment below in conjunction with the accompanying drawings.
Embodiment
A kind of modified model hydrogen peroxide mixing bubble systems, its structure is as it is shown in figure 1, include source of the gas 1, defecator
2, air inlet pipe 8 and container 7, hydrogen peroxide is located in container 7, and air inlet pipe 8 extend in container 7, the other end
It is connected with source of the gas 1 through defecator 3.Wherein, air inlet pipe 8 is L-shaped structure, by interconnective vertical duct
Body 81 and horizontal pipe shaft 82 are constituted, and vertical pipe shaft 81 extend into the bottom of container 7, and horizontal pipe shaft 82 is laid on
On the bottom surface of container 7, the end seal of air inlet pipe 8, vertical pipe shaft 81 and horizontal pipe shaft 82 are provided with multiple
Venthole 9, in addition, the horizontal pipe shaft 82 being laid on container bottoms is also associated with several perpendicular
The branched pipe 83 arranged, branched pipe 83 is also equipped with venthole 9.
Below the structure of air inlet pipe 8 is described further: vertical pipe shaft 81 difference towards on be equipped with out
Pore 9, the aperture of the venthole of top is less, generally 2mm, and the spacing between each venthole is 10cm,
The venthole aperture of lower section is relatively big, and generally 3mm, the spacing between each venthole is 5cm.The most permissible
Avoid the problem that gas can not enter bottom.Laterally the venthole on pipe shaft 82 is 45 ° of direction perforates obliquely,
The aperture of venthole is 3mm, and the spacing between each venthole is 5cm.Venthole on branched pipe 83 is 45 °
Direction perforate obliquely, the aperture of venthole is 2mm, and the spacing between each venthole is 10cm.The position of perforate
Put and size has highly important impact for hydrogen peroxide mixed effect in container, utilize the compression discharged empty
Gas carries out forced convertion, makes dioxygen water body through main diffusion, eddy diffusivity mix homogeneously, is initially formed large scale
Vortex micelle, in turbulent flow stretching, under shear action, maelstrom splits into the vortex of smaller scale, and energy is from maelstrom
Being delivered to little vortex, little vortex then to less vortex transmission, finally realizes mix homogeneously.
In addition, it is connected between source of the gas 1 with defecator 3 and has the dew preventing moisture in gas phase from entering in hydrogen peroxide
Point supervising device 2.The pipeline that defecator 3 is connected with container 7 is provided with interval bubbling and controls valve 6 and pressure
Alarm device 5.Defecator 3 is also associated with Backwash pipeline, the two ends of this pipeline respectively with defecator
Pipeline between 3 and defecator 3 with container 7 is connected, and arranges back flush valves 4 in Backwash pipeline.
The recoil wiper mechanism being arranged on defecator 3 side is utilized periodically to go the removal of impurity, (such as can be each
Hour recoil valve can automatic backflushing according to program).Pressure warning unit 5 can detect the pressure in pipeline, and root
According to setting value can the number of delivering a letter to middle control.Intermittently bubbling control valve 6 makes mixing more efficient uniformly, (can be as required
Set and open 10 seconds as per minute, reach an effect surged).
It addition, the defecator 3 used is particle filtering unit, drying unit and the activated carbon adsorption being sequentially connected with
The three-level filter device of unit, particle filtering unit is multiple stage filter units, may filter that more than diameter 0.01 μm
Granule, follow-up drying unit and activated carbon adsorption unit remove moisture in air further, it is ensured that hydrogen peroxide
Degree of purity, it is to avoid introduce impurity effect degree of purity, and the pressure of more convenient control bubbling in hydrogen peroxide product.
Claims (10)
1. a modified model hydrogen peroxide mixing bubble systems, including source of the gas, defecator, air inlet pipe and container,
Described hydrogen peroxide is located in container, and described air inlet pipe extend in container, and the other end is through defecator and source of the gas
Connect, it is characterised in that
Described air inlet pipe is L-shaped structure, vertically extend into the bottom of container, is laterally laid on container bottoms,
The end seal of air inlet pipe, pipe shaft is provided with multiple venthole.
A kind of modified model hydrogen peroxide mixing bubble systems the most according to claim 1, it is characterised in that paving
It is located in the transverse pipe on container bottoms the branched pipe being also associated with several perpendicular setting, this branched pipe is arranged
There is venthole.
A kind of modified model hydrogen peroxide mixing bubble systems the most according to claim 1, it is characterised in that perpendicular
To pipe shaft difference towards on be equipped with venthole, the venthole aperture of top is less, the spacing between each venthole
Relatively big, the venthole aperture of lower section is relatively big, and the spacing between each venthole is less.
A kind of modified model hydrogen peroxide mixing bubble systems the most according to claim 3, it is characterised in that on
The aperture of the venthole of side is 2mm, and the spacing between each venthole is 10cm, and the aperture of the venthole of lower section is
3mm, the spacing between each venthole is 5cm.
A kind of modified model hydrogen peroxide mixing bubble systems the most according to claim 1, it is characterised in that horizontal
Venthole on pipe shaft is 45 ° of direction perforates obliquely, and the aperture of venthole is 3mm, between each venthole
Spacing be 5cm.
A kind of modified model hydrogen peroxide mixing bubble systems the most according to claim 2, it is characterised in that point
Venthole on arm is 45 ° of direction perforates obliquely, and the aperture of venthole is 2mm, between each venthole
Spacing is 10cm.
A kind of modified model hydrogen peroxide mixing bubble systems the most according to claim 1, it is characterised in that institute
It is connected between the source of the gas stated and defecator and has the dew point supervising device prevented in gas phase in moisture entrance hydrogen peroxide.
A kind of modified model hydrogen peroxide mixing bubble systems the most according to claim 1, it is characterised in that institute
The pipeline that the defecator stated is connected with container is provided with interval bubbling and controls valve and pressure warning unit.
A kind of modified model hydrogen peroxide mixing bubble systems the most according to claim 1, it is characterised in that institute
Be also associated with Backwash pipeline on the defecator stated, the two ends of this pipeline respectively with defecator and defecator with
Pipeline between container connects, and arranges back flush valves in Backwash pipeline.
A kind of modified model hydrogen peroxide mixing bubble systems the most according to claim 1, it is characterised in that institute
The defecator stated is the three-stage filtration of the particle filtering unit, drying unit and the activated carbon adsorption unit that are sequentially connected with
Device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510026370.7A CN105854718A (en) | 2015-01-19 | 2015-01-19 | Improved hydrogen peroxide mixing bubbling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510026370.7A CN105854718A (en) | 2015-01-19 | 2015-01-19 | Improved hydrogen peroxide mixing bubbling system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105854718A true CN105854718A (en) | 2016-08-17 |
Family
ID=56622885
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510026370.7A Pending CN105854718A (en) | 2015-01-19 | 2015-01-19 | Improved hydrogen peroxide mixing bubbling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105854718A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110052204A (en) * | 2019-05-28 | 2019-07-26 | 中煤科工集团重庆研究院有限公司 | One kind being used for coal mine multiphase slurries mixed airflow agitating device |
-
2015
- 2015-01-19 CN CN201510026370.7A patent/CN105854718A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110052204A (en) * | 2019-05-28 | 2019-07-26 | 中煤科工集团重庆研究院有限公司 | One kind being used for coal mine multiphase slurries mixed airflow agitating device |
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Legal Events
| Date | Code | Title | Description |
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| C06 | Publication | ||
| PB01 | Publication | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20160817 |