CN106621882A - Gas mixing device - Google Patents
Gas mixing device Download PDFInfo
- Publication number
- CN106621882A CN106621882A CN201611076654.8A CN201611076654A CN106621882A CN 106621882 A CN106621882 A CN 106621882A CN 201611076654 A CN201611076654 A CN 201611076654A CN 106621882 A CN106621882 A CN 106621882A
- Authority
- CN
- China
- Prior art keywords
- tower body
- gas
- separating device
- discharge outlet
- guide plate
- 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.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
- B01F23/23105—Arrangement or manipulation of the gas bubbling devices
- B01F23/2311—Mounting the bubbling devices or the diffusers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
- B01F23/23105—Arrangement or manipulation of the gas bubbling devices
- B01F23/2311—Mounting the bubbling devices or the diffusers
- B01F23/23112—Mounting the bubbling devices or the diffusers comprising the use of flow guiding elements adjacent or above the gas stream
- B01F23/231121—Mounting the bubbling devices or the diffusers comprising the use of flow guiding elements adjacent or above the gas stream the flow guiding elements being baffles, tubes or walls
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/421—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path
- B01F25/423—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path by means of elements placed in the receptacle for moving or guiding the components
- B01F25/4231—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path by means of elements placed in the receptacle for moving or guiding the components using baffles
Abstract
The invention provides a gas mixing device. The gas mixing device comprises a tower body, wherein an aeration device is arranged in the tower body; a gas exhaust port is formed in the upper part of the tower body; at least one partition device is arranged between the aeration device and the gas exhaust port and divides the tower body into curved chambers. Gas rises along the curved path between the aeration device and the gas exhaust port. According to the gas mixing device, the curved chambers are formed in the tower body through change of the arrangement of space in the tower body, the gas ascending path is prolonged, accordingly, the contact time of gas and a liquid is prolonged, the dissolvability of gas and the liquid is greatly improved, the concentration of dissolved gas can be guaranteed in a limited space, the height of the tower body is reduced, and cost control is facilitated.
Description
Technical field
The present invention relates to gas mixing technology field, more particularly to a kind of gas mixer.
Background technology
At present existing gas mixer is dissolved after aeration by the way of contacting naturally, generally,
The solubility of gas is directly proportional to the height of gas mixer, and the height higher dissolving time of contact of gas mixer is more
It is long, therefore the gas concentration of ordinary dissolution for obtaining is higher.However, the height of having no limits that cannot be done due to the restriction of factory height
Degree, cannot meet higher gas concentration of ordinary dissolution under same floor space and height, and factory building height is more high undoubtedly can
Building cost is set to be multiplied.
The content of the invention
Based on this, the invention reside in providing a kind of gas mixer, it can improve the solubility of gas, and not increase
The height of gas mixer.
Its technical scheme is as follows:
A kind of gas mixer, including tower body, are provided with aerator in the tower body, the top of the tower body is provided with
Gas discharge outlet, is provided with least one separating device, the separation dress between the aerator and the gas discharge outlet
Put the separation tower body and form curved chamber.
A kind of gas mixer, including tower body, are provided with aerator in the tower body, the top of the tower body is provided with
Gas discharge outlet, gas rises between the aerator and the gas discharge outlet along curved path.
Further technical scheme is illustrated below:
In one of embodiment, the separating device separates the tower body and forms S die cavities room.
In one of embodiment, separating device described at least two is included, the two neighboring separating device replaces
It is fixed on the opposite face of the tower body inwall.
In one of embodiment, the separating device to the gas discharge outlet is inclined.
In one of embodiment, angle of inclination from the separating device to the gas discharge outlet for the scope of α be 3 °-
15°。
In one of embodiment, the separating device includes fixed station and guide plate, and the fixed station is fixed on described
Tower body inwall and match with the wall configuration of the tower body, the guide plate is placed on the fixed station.
In one of embodiment, the guide plate the tower body transverse projection length be L, the tower body it is horizontal
The D of width, 1/2D < L≤2/3D.
In one of embodiment, the guide plate is shaped as arc away from one end of the fixed station.
In one of embodiment, the guide plate the tower body transverse projection length be L, the diameter of the tower body
For D, L=2/3D.
Principle, effect below to preceding solution etc. are illustrated:
Above-mentioned gas mixing arrangement is arranged by changing the space inside tower body, makes tower body be internally formed curved chamber, gas
The restriction of minute bubbles floating and the curved chamber due to tower body that body is formed by the aerator, and effectively extend gas
Floating path, makes gas extend with the time of contact of liquid, substantially increases the solubility of gas and liquid such that it is able to having
The concentration of ordinary dissolution of gas is guaranteed in the space of limit, the height of tower body is reduced, beneficial to the control of cost.The gas mixer leads to
Cross and the separating device is set between aerator and gas discharge outlet, separated in the tower body by the separating device
Portion space and form the curved chamber, when gas floats, the gas of floating runs into and can change after the separating device direction
Float, so as to extend the time of contact of gas and liquid.
Description of the drawings
Fig. 1 is the structural representation of gas mixer of the present invention.
Description of reference numerals:
100th, tower body, 110, gas discharge outlet, 120, separating device, 122, fixed station, 124, guide plate, 140, feed liquor
Mouthful, 142, shower nozzle, 200, aerator.
Specific embodiment
Embodiments of the invention are described in detail below:
As shown in figure 1, a kind of gas mixer, including tower body 100, aerator is provided with the tower body, it is described
The top of tower body 100 is provided with gas discharge outlet 110, be provided between the aerator 120 and the gas discharge outlet 110 to
A few separating device 120, the separating device 120 separates the tower body 100 and forms curved chamber.Or by controlling gas
Floating path, and make gas between the aerator 200 and the gas discharge outlet 110 along curved path rise.
The gas mixer is arranged by changing the space inside tower body 100, makes tower body 100 be internally formed curved chamber
Room, the minute bubbles floating that gas is formed by the aerator 200 and the restriction (gas of the curved chamber due to tower body 100
Direction shown in arrow in tower body 100 in the floating direction such as Fig. 1 of body), and effectively extend gas floating path, make gas and liquid
Time of contact extend, substantially increase the solubility of gas and liquid such that it is able to guarantee gas in limited space
Concentration of ordinary dissolution, reduces the height of tower body 100, beneficial to the control of cost.The gas mixer by aerator 200 with
The separating device 120 is set between gas discharge outlet 110, the inside of the tower body 100 is separated by the separating device 120
Space and form the curved chamber, when gas floats, the gas of floating runs into and can change after the separating device 120 direction
Float, so as to extend the time of contact of gas and liquid.
The separating device 200 separates the tower body 100 and forms S die cavities room.In same height space, the S types
Chamber can effectively extend the path of gas floating, and compared with conventional gas mixer, the tower body 100 of S die cavities room can make
The floating path of gas extends at least one times.Requirement that can be according to user to the solubility of gas, arranges and multiple described separates dress
200 are put, and forms multiple continuous S die cavities rooms, it is also possible to form undaform chamber, can equally reach prolongation gas floating road
The purpose in footpath.
As shown in figure 1, the gas mixer includes separating device 120 described at least two, it is two neighboring described
Separating device 120 is alternately fixed on the opposite face of the inwall of the tower body 100.The gas that aerator 120 is formed is in floating-upward process
In, but when running into first separating device 120, gas changes floating direction and continues to float for the first time, can run into afterwards
Second separating device 120, the 3rd separating device 120 ... separating device 120 described in n-th, until gas
Discharge from the gas discharge outlet 110, and do not run into a separating device 120, gas can then change direction of once floating,
Floating path is extended with this.Multiple separating devices 120 can be uniformly or non-uniformly arranged in the tower body 100, and adjacent two
Spacing between the individual separating device 120 can also according to user like be set to it is equal or unequal.
The separating device 120 to the gas discharge outlet 110 is inclined.When gas runs into described point during floating
When device 120, floating path can be changed, and separating device 120 described in 120 for being obliquely installed can effectively guide the floating of gas
Direction.It is preferred that the separating device 120 is 3 ° -15 ° for the scope of α to the angle of inclination of the gas discharge outlet.Can according to
Requirement of the family to gas solubility, α selects appropriate angle, and α more atmospheric solubility is relatively lower.
The separating device 120 includes fixed station 122 and guide plate 124, and the fixed station 122 is fixed on the tower body
100 inwalls and match with the wall configuration of the tower body 100, the guide plate 124 is placed on the fixed station 122.It is described
The shape of tower body 100 can be cylinder, elliptical cylinder-shape, rectangle cylindricality etc., and accordingly, the wall configuration of the tower body 100 can be
Circular arc, ellipse arc, fold-line-shaped;And the guide plate 124 is placed on the fixed station 122, so to the fixed station
122 length, width have certain requirement, and the shape of part that the guide plate 124 coordinates with the fixed station 122
It is adapted with the shape of the fixed station 122.It is preferred that shape of the guide plate 124 away from one end of the fixed station 122
It is adapted with the shape of the tower body 100.One end that guide plate 124 described in the present embodiment is engaged with the fixed station 122 and
Arc is away from one end of the fixed station 122.
Guide plate 124 and the movable fit system of fixed station 122, are easy to installation, the maintenance of tower body 100 of guide plate 124,
And for the requirement of same gas mixer gas with various solubility, the guide plate 124 that may be selected to arrange varying number and
The diverse location of tower body 100 arranges guide plate 124.The guide plate 124 to the gas discharge outlet 110 is inclined, inclined angle alpha
Scope is 3 ° -15 °, the fixed station 122 may be selected and is arranged in the way of inclining 3 ° -15 ° to the gas discharge outlet 110, no
Only stablizing beneficial to the guide plate 124, and simple structure;It is of course also possible to select other modes to make the guide plate 124
Incline to the gas discharge outlet 110.
Further, the inlet 140 for entering for liquid is provided with the tower body 100, liquid enters from the inlet 140
After entering, sprayed by shower nozzle 142, preferably the separating device 120 is located between the aerator 200 and the shower nozzle 142.
The guide plate 124 the tower body 100 transverse projection length be L, the D of the transverse width of the tower body 100,
1/2D < L≤2/3D.When the tower body 100 is cylinder, the transverse width of the tower body 100 is the tower body 100
Diameter, i.e., the projected length in the diametric(al) of the tower body 100 of described guide plate 124 is L.The present embodiment preferably L
=2/3D.
Each technical characteristic of embodiment described above can be combined arbitrarily, to make description succinct, not to above-mentioned reality
Apply all possible combination of each technical characteristic in example to be all described, as long as however, the combination of these technical characteristics is not deposited
In contradiction, the scope of this specification record is all considered to be.
Embodiment described above only expresses the several embodiments of the present invention, and its description is more concrete and detailed, but and
Can not therefore be construed as limiting the scope of the patent.It should be pointed out that for one of ordinary skill in the art comes
Say, without departing from the inventive concept of the premise, some deformations and improvement can also be made, these belong to the protection of the present invention
Scope.Therefore, the protection domain of patent of the present invention should be defined by claims.
Claims (10)
1. a kind of gas mixer, it is characterised in that including tower body, aerator, the tower body are provided with the tower body
Top be provided with gas discharge outlet, at least one separating device is provided between the aerator and the gas discharge outlet,
The separating device separates the tower body and forms curved chamber.
2. gas mixer according to claim 1, it is characterised in that the separating device separates the tower body and formed
S die cavities room.
3. gas mixer according to claim 1, it is characterised in that include separating device described at least two,
The two neighboring separating device is alternately fixed on the opposite face of the tower body inwall.
4. the gas mixer according to claims 1 to 3 any one, it is characterised in that the separating device is to institute
State gas discharge outlet inclination.
5. gas mixer according to claim 4, it is characterised in that the separating device is to the gas discharge outlet
Angle of inclination be 3 ° -15 ° for the scope of α.
6. the gas mixer according to claims 1 to 3 any one, it is characterised in that the separating device includes
Fixed station and guide plate, the fixed station is fixed on the tower body inwall and matches with the wall configuration of the tower body, described
Guide plate is placed on the fixed station.
7. gas mixer according to claim 6, it is characterised in that horizontal throwing of the guide plate in the tower body
Shadow length is L, the D of the transverse width of the tower body, 1/2D < L≤2/3D.
8. gas mixer according to claim 6, it is characterised in that the guide plate away from the fixed station one
That what is held is shaped as arc.
9. gas mixer according to claim 8, it is characterised in that horizontal throwing of the guide plate in the tower body
Shadow length is L, a diameter of D, L=2/3D of the tower body.
10. a kind of gas mixer, it is characterised in that including tower body, aerator, the tower body are provided with the tower body
Top be provided with gas discharge outlet, gas rises between the aerator and the gas discharge outlet along curved path.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611076654.8A CN106621882A (en) | 2016-11-28 | 2016-11-28 | Gas mixing device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611076654.8A CN106621882A (en) | 2016-11-28 | 2016-11-28 | Gas mixing device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN106621882A true CN106621882A (en) | 2017-05-10 |
Family
ID=58813193
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201611076654.8A Pending CN106621882A (en) | 2016-11-28 | 2016-11-28 | Gas mixing device |
Country Status (1)
Country | Link |
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CN (1) | CN106621882A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108128891A (en) * | 2018-01-11 | 2018-06-08 | 鲁东大学 | A kind of novel energy-saving is aerated pool device |
CN110237734A (en) * | 2019-06-10 | 2019-09-17 | 中国石油大学(北京) | Gas mixer and emission-control equipment |
CN111298161A (en) * | 2019-12-09 | 2020-06-19 | 河北华沃环保科技有限责任公司 | Deodorization sterilizing equipment based on ozone and odorless garbage room with same |
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2016
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CN1736903A (en) * | 2005-07-20 | 2006-02-22 | 天津大学 | Method and device promoting gas dissolution through subaqueous aeration |
CN201120258Y (en) * | 2007-11-14 | 2008-09-24 | 梁卫宁 | Dissolution assisting device |
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CN101716448A (en) * | 2010-01-04 | 2010-06-02 | 中国科学院过程工程研究所 | Dynamic rotary rotational flow plate device for strengthening transmission |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108128891A (en) * | 2018-01-11 | 2018-06-08 | 鲁东大学 | A kind of novel energy-saving is aerated pool device |
CN110237734A (en) * | 2019-06-10 | 2019-09-17 | 中国石油大学(北京) | Gas mixer and emission-control equipment |
CN111298161A (en) * | 2019-12-09 | 2020-06-19 | 河北华沃环保科技有限责任公司 | Deodorization sterilizing equipment based on ozone and odorless garbage room with same |
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PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
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Application publication date: 20170510 |