CN205965548U - A blending tank for gas -liquid two -phase reaction - Google Patents
A blending tank for gas -liquid two -phase reaction Download PDFInfo
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- CN205965548U CN205965548U CN201621011106.2U CN201621011106U CN205965548U CN 205965548 U CN205965548 U CN 205965548U CN 201621011106 U CN201621011106 U CN 201621011106U CN 205965548 U CN205965548 U CN 205965548U
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- tank
- deflector
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Abstract
The utility model discloses a blending tank for gas -liquid two -phase reaction, including a jar body, the top of jar body is equipped with liquid inlet, and the bottom is equipped with mixed liquid outlet, the inner wall of the jar body is equipped with spiral helicine guide plate, and two should be no less than to the quantity of spiral, the internal gas -supply pipe that extends on its axis that is equipped with of jar, the surface of this gas -supply pipe is equipped with and is the venthole that the same helical configuration distributes with the guide plate, the top and the air inlet intercommunication of setting on jar body upper portion of gas -supply pipe, the bottom is sealed. The utility model discloses simple structure, reasonable in design utilizes the cooperation of spiral helicine guide plate and gas -supply pipe, makes jar internal liquid and gas mixing even, subsequent technology gets into and in the reaction more abundant.
Description
Technical field
This utility model is related to a kind of Liqiud-gas mixing device, especially relates to a kind of mixing for gas-liquid two-phase reaction
Tank.
Background technology
In medication chemistry manufacturing enterprise, in order to separate mixed gas with obtain certain component, remove harmful components with
Purification gas, prepare solution of certain gas etc. and have to use Liqiud-gas mixing device, need bubble or other gas
It is mixed in liquid to be acted upon to it.And traditional Liqiud-gas mixing device then has certain deficiency, for example：Device
Internal structure is complicated, generally will mate power agitating device, additionally it has been difficult to guarantee gas and liquid are sufficiently mixed.
Utility model content
For problems of the prior art, this utility model provides a kind of mixing for gas-liquid two-phase reaction
Tank, in conjunction with simple, reasonable in design, promote the liquid in tank body uniform with gas mixing, enter in follow-up technique and react more
Fully.
The concrete technical scheme that this utility model is adopted is as follows：
A kind of blending tank for gas-liquid two-phase reaction, including tank body, the top of tank body is provided with liquid inlet, and bottom is provided with
Mixture export；
The inwall of described tank body is provided with spiral helicine deflector, and the quantity of spiral should be no less than two；
The appendix extend is provided with described tank body on axis wherein, it is in phase that the surface of this appendix is provided with deflector
Venthole with helicoidal structure distribution；
The top of described appendix is connected with the air inlet being arranged on tank body top, bottom end closure.
For lifting the effect of gas-liquid mixed further, as preferred, the bottom bore of described tank body is towards described mixed liquor
Outlet gradually restrains, and that is, tank base internal diameter is gradually reduced, and mixture export is located at minimum bore.
As preferred, the height of described deflector is equal to 0.5～0.8 times of tank inner chamber radius.；If deflector mistake
Little, it is unfavorable for that liquid flows around deflector, mixed effect is poor；The installation of appendix if highly excessive, can be affected.
This utility model structure is simple, reasonable in design, using the cooperation of spiral helicine deflector and appendix, promotes tank body
Interior liquid with gas mixing uniformly, enters in follow-up technique and reacts more abundant.
Brief description
Fig. 1 is the structure chart of blending tank in this utility model.
Specific embodiment
A kind of blending tank for gas-liquid two-phase reaction as shown in Figure 1, including tank body 1, the top of tank body is provided with liquid
Entrance 2, bottom is provided with mixture export 3.
In the present embodiment, the bottom bore of tank body 1 is gradually restrained towards mixture export 3, and that is, tank base internal diameter gradually subtracts
Little, mixture export 3 is located at lowest calibre, the specifically convergence position 8 in visible Fig. 1.
The inwall of tank body 1 is provided with spiral helicine deflector 4, and the quantity of spiral should be no less than two, further, spiral
Quantity is 2～5, is more beneficial for gas and liquid is sufficiently mixed, little to liquid mobile obstacle.
The appendix 5 extend is provided with tank body 1 on axis wherein, it is in phase that the surface of this appendix 5 is provided with deflector 4
With the venthole 6 of helicoidal structure distribution, and the top of this appendix is connected with the air inlet 7 being arranged on tank body top, bottom
Closing.
In the present embodiment, the height of deflector 4 is equal to 0.5～0.8 times of tank inner chamber radius；If deflector is too small, no
Flow around deflector beneficial to liquid, mixed effect is poor；The installation of appendix if highly excessive, can be affected.
The work process of above-mentioned Liqiud-gas mixing device is as follows：
Liquid to be mixed enters in tank body 1 through liquid inlet 2, and gas enters in appendix 5 by air inlet 7, liquid
Flow to mixture export 3 along deflector 4, during flowing, be sufficiently mixed with venthole 6 expellant gas, and by mixing
Liquid outlet 3 enters in subsequent processing or reactor.
The foregoing is only preferable implementation example of the present utility model, be not limited to this utility model, all in this reality
Within new spirit and principle, any modification, equivalent substitution and improvement made etc., should be included in guarantor of the present utility model
Within the scope of shield.
Claims (3)
1. a kind of blending tank for gas-liquid two-phase reaction is it is characterised in that include tank body, the top of tank body is provided with liquid and enters
Mouthful, bottom is provided with mixture export；
The inwall of described tank body is provided with spiral helicine deflector, and the quantity of spiral should be no less than two；
The appendix extend is provided with described tank body on axis wherein, it is in identical spiral shell that the surface of this appendix is provided with deflector
The venthole of rotation shape structure distribution；
The top of described appendix is connected with the air inlet being arranged on tank body top, bottom end closure.
2. blending tank as claimed in claim 1 it is characterised in that described tank body bottom bore towards described mixture export by
Taper and hold back.
3. blending tank as claimed in claim 2 is it is characterised in that the height of described deflector is equal to tank inner chamber radius
0.5～0.8 times.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621011106.2U CN205965548U (en) | 2016-08-30 | 2016-08-30 | A blending tank for gas -liquid two -phase reaction |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621011106.2U CN205965548U (en) | 2016-08-30 | 2016-08-30 | A blending tank for gas -liquid two -phase reaction |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205965548U true CN205965548U (en) | 2017-02-22 |
Family
ID=58039227
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621011106.2U Active CN205965548U (en) | 2016-08-30 | 2016-08-30 | A blending tank for gas -liquid two -phase reaction |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205965548U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110756072A (en) * | 2019-11-06 | 2020-02-07 | 中国石油天然气股份有限公司 | Mixing device and mixing method for oil-gas mixed transportation of oilfield associated gas |
| CN112584918A (en) * | 2018-08-10 | 2021-03-30 | 斯塔克拉博公司 | Device for contacting a gas stream with a liquid stream |
| CN114225728A (en) * | 2021-12-29 | 2022-03-25 | 北京美斯顿科技开发有限公司 | Mixer and waste liquid treatment equipment |
-
2016
- 2016-08-30 CN CN201621011106.2U patent/CN205965548U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112584918A (en) * | 2018-08-10 | 2021-03-30 | 斯塔克拉博公司 | Device for contacting a gas stream with a liquid stream |
| CN112584918B (en) * | 2018-08-10 | 2023-02-10 | 斯塔克拉博公司 | Device for contacting a gas stream with a liquid stream |
| US11654391B2 (en) | 2018-08-10 | 2023-05-23 | Starklab | Device for bringing a gas stream and a liquid stream into contact |
| CN110756072A (en) * | 2019-11-06 | 2020-02-07 | 中国石油天然气股份有限公司 | Mixing device and mixing method for oil-gas mixed transportation of oilfield associated gas |
| CN110756072B (en) * | 2019-11-06 | 2024-03-05 | 中国石油天然气股份有限公司 | Mixing device and mixing method for oilfield associated gas and oil gas mixed transportation |
| CN114225728A (en) * | 2021-12-29 | 2022-03-25 | 北京美斯顿科技开发有限公司 | Mixer and waste liquid treatment equipment |
| CN114225728B (en) * | 2021-12-29 | 2022-12-02 | 北京美斯顿科技开发有限公司 | Mixer and waste liquid treatment equipment |
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| GR01 | Patent grant |