CN106621882A - Gas mixing device - Google Patents

Gas mixing device Download PDF

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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
Application number
CN201611076654.8A
Other languages
Chinese (zh)
Inventor
付巧明
朱定洲
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guangzhou Tech Long Packaging Machinery Co Ltd
Original Assignee
Guangzhou Tech Long Packaging Machinery Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Guangzhou Tech Long Packaging Machinery Co Ltd filed Critical Guangzhou Tech Long Packaging Machinery Co Ltd
Priority to CN201611076654.8A priority Critical patent/CN106621882A/en
Publication of CN106621882A publication Critical patent/CN106621882A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105Arrangement or manipulation of the gas bubbling devices
    • B01F23/2311Mounting the bubbling devices or the diffusers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105Arrangement or manipulation of the gas bubbling devices
    • B01F23/2311Mounting the bubbling devices or the diffusers
    • B01F23/23112Mounting the bubbling devices or the diffusers comprising the use of flow guiding elements adjacent or above the gas stream
    • B01F23/231121Mounting 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/42Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/421Static 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
    • B01F25/423Static 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
    • B01F25/4231Static 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

Gas mixer
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.
CN201611076654.8A 2016-11-28 2016-11-28 Gas mixing device Pending CN106621882A (en)

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

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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
CN (1) CN106621882A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
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

Citations (7)

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Publication number Priority date Publication date Assignee Title
CN1736903A (en) * 2005-07-20 2006-02-22 天津大学 Method and device promoting gas dissolution through subaqueous aeration
US20080035226A1 (en) * 1994-11-04 2008-02-14 Conrad Wayne E Fluid contact chamber
CN201120258Y (en) * 2007-11-14 2008-09-24 梁卫宁 Dissolution assisting device
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
CN102131572A (en) * 2008-08-26 2011-07-20 松下电工株式会社 Air-dissolved water production device
US20150352505A1 (en) * 2013-01-31 2015-12-10 Kabushiki Kaisha Yokota Seisakusho Gas-liquid dissolving tank and microscopic bubble generator
CN206295835U (en) * 2016-11-28 2017-07-04 广州达意隆包装机械股份有限公司 Gas mixer

Patent Citations (7)

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Publication number Priority date Publication date Assignee Title
US20080035226A1 (en) * 1994-11-04 2008-02-14 Conrad Wayne E Fluid contact chamber
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
CN102131572A (en) * 2008-08-26 2011-07-20 松下电工株式会社 Air-dissolved water production device
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
US20150352505A1 (en) * 2013-01-31 2015-12-10 Kabushiki Kaisha Yokota Seisakusho Gas-liquid dissolving tank and microscopic bubble generator
CN206295835U (en) * 2016-11-28 2017-07-04 广州达意隆包装机械股份有限公司 Gas mixer

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Title
姚运先: "《室内环境污染控制》", 30 June 2007, 中国环境科学出版社 *

Cited By (3)

* Cited by examiner, † Cited by third party
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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Application publication date: 20170510