CN102489138A - Absorbing tower with liquid self-flowing and stirring - Google Patents
Absorbing tower with liquid self-flowing and stirring Download PDFInfo
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- CN102489138A CN102489138A CN2011104456077A CN201110445607A CN102489138A CN 102489138 A CN102489138 A CN 102489138A CN 2011104456077 A CN2011104456077 A CN 2011104456077A CN 201110445607 A CN201110445607 A CN 201110445607A CN 102489138 A CN102489138 A CN 102489138A
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- valve
- circulating pump
- absorption tower
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Abstract
The invention discloses an absorbing tower with liquid self-flowing and stirring, and is a chemical production device which can solve the problem of stirring technology of liquid in the production process. According to a technical scheme of the invention, a liquid inlet general pipeline (2) is provided at periphery of the absorbing tower (1), a plurality of tower entrance pipelines (3) are connected on the general pipeline, bends (4) are provided at the heads of the tower entrance pipelines, a valve (5) and a valve (6) are arranged on the liquid inlet general pipeline, a pipeline (7) enables connection between the two valves, and is connected with a circulating pump (8), the circulating pump is connected to a motor (9), a pipeline (10) at the lower part of the circulating pump is introduced in the absorbing tower, and a valve (11) is arranged on the pipeline. The product of the invention can be used for producing ammonium fluosilicate.
Description
Technical field
The present invention discloses a kind of absorption tower, the absorption tower that a kind of specifically carrying liqs gravity flow is stirred.
Background technology
The absorption tower is a kind of equipment commonly used in the Chemical Manufacture, its structure, and occupation mode is a lot.The correlation technique of having applied for national patent is quite a few, is that 201120111944.8 " adopting tower prime cement liquid pool to continue the Gas-Liquid Absorption device of overflow " promptly is one of a kind of representative like application number.
Because different Chemical Manufacture objects need use the differing absorption tower according to the production technology configuration, therefore, all there is a kind of evolution of lasting innovation in this type technology.
, ammonium fluoride becomes in the production process of ammonium fluosilicate after absorbing fluorinated tail gas, the especially significant of the improvement in performance on its absorption tower, otherwise adopt prior art equipment; Ammonium fluosilicate solution cooling back easy and crystalline; At the bottom of the deposition tower, the influence circulation absorbs, and is seriously restricting production efficiency and product quality.
Summary of the invention
Goal of the invention of the present invention just provides a kind of absorption tower that in the process of production liquid flows, keeps agitating function.
Realize that technical scheme of the present invention is such: the absorption tower that the carrying liqs gravity flow is stirred; Structure is followed many at the total pipeline first line of a couplet and is gone into tower pipeline 3 for 1 periphery is provided with feed liquor total pipeline 2 on the absorption tower, and the head of going into the tower pipeline is equipped with elbow 4; Valve 5 and valve 6 are installed on the feed liquor total pipeline; Between valve 5 and valve 6, connecting pipeline 7, connecting with circulating pump 8, circulating pump is connecting motor 9, in the pipeline 10 feeding absorption towers under the circulating pump, valve 11 is installed on it.
When going into tower pipeline 3 entering absorption towers 1 certain setting angle is arranged all, can be 10 degree～80 degree; Its elbow 4 can unify to be arranged to clockwise direction or counter clockwise direction.
Beneficial effect of the present invention is: impact through pump discharge, under special angle, material forms the whirlpool stirring in the tower, thereby makes the material that contains certain crystal be in suspended state, is unlikely to crystallization and piles up, and influences assimilation effect; Next has realized that the on-mechanical under the airtight condition stirs, and has simplified the structure and investment use cost of equipment, significantly improves the comprehensive benefit of production.
Description of drawings
Fig. 1 is a structural representation front view of the present invention;
Fig. 2 is a structural representation vertical view of the present invention.
Among each figure, the 1st, absorption tower, the 2nd, feed liquor total pipeline, the 3rd is gone into tower pipeline, the 4th, elbow, the 5th, valve, the 6th, valve, the 7th, pipeline, the 8th, circulating pump, the 9th, motor, the 10th, pipeline, the 11st, valve.
The specific embodiment
Below in conjunction with the explanation of accompanying drawing specific embodiments of the invention as follows:
Embodiment 1: the absorption tower that the carrying liqs gravity flow is stirred
Concrete structure is for 1 periphery is provided with feed liquor total pipeline 2 on the absorption tower; Follow four at the total pipeline first line of a couplet and go into tower pipeline 3; The head of respectively going into the tower pipeline is equipped with elbow 4, and valve 5 and valve 6 are installed on the feed liquor total pipeline, between valve 5 and valve 6, is connecting pipeline 7, is connecting with circulating pump 8; Circulating pump is connecting motor 9, in the pipeline 10 feeding absorption towers under the circulating pump, valve 11 is installed on it.
When going into tower pipeline 3 entering absorption towers 1 certain setting angle is arranged all, pipeline and Ta Bi have 30 ° of inclinations angle when being about to insert in the tower into the tower pipeline, and all go into the elbow 4 unified clockwise directions that are arranged to of tower pipeline, and are high 15 centimetres at the bottom of tower.
Embodiment 2: the absorption tower that the carrying liqs gravity flow is stirred
Concrete structure is for 1 periphery is provided with feed liquor total pipeline 2 on the absorption tower; Follow the six roots of sensation at the total pipeline first line of a couplet and go into tower pipeline 3; The head of respectively going into the tower pipeline is equipped with elbow 4, and valve 5 and valve 6 are installed on the feed liquor total pipeline, between valve 5 and valve 6, is connecting pipeline 7, is connecting with circulating pump 8; Circulating pump is connecting motor 9, in the pipeline 10 feeding absorption towers under the circulating pump, valve 11 is installed on it.
When going into tower pipeline 3 entering absorption towers 1 certain setting angle is arranged all, pipeline and Ta Bi have 50 ° of inclinations angle when being about to insert in the tower into the tower pipeline, and all go into elbow 4 unified being arranged to counterclockwise of tower pipeline, and are high 30 centimetres at the bottom of tower.
Stirring the pump parameters is: flow 30m
2/ h, lift: 30m, power of motor: 15kW.
Claims (2)
1. the absorption tower of carrying liqs gravity flow stirring includes the absorption tower, pipeline; Valve, circulating pump, motor; It is characterized in that: the periphery of (1) is provided with feed liquor total pipeline (2) on the absorption tower, follows many at the total pipeline first line of a couplet and goes into tower pipeline (3), and the head of going into the tower pipeline is equipped with elbow (4); Valve (5) and valve (6) are installed on the feed liquor total pipeline; Between valve (5) and valve (6), connecting pipeline (7), connecting with circulating pump (8), circulating pump is connecting motor (9), and the pipeline under the circulating pump (10) feeds in the absorption tower, valve (11) is installed on it.
2. liquid flows agitator according to claim 1 is characterized in that: go into tower pipeline (3) and get into the certain setting angle of absorption tower (1) Shi Junyou, can be 10 degree～80 degree, the height of its outlet at the bottom of the tower is 15 centimetres to 30 centimetres.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011104456077A CN102489138A (en) | 2011-12-28 | 2011-12-28 | Absorbing tower with liquid self-flowing and stirring |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011104456077A CN102489138A (en) | 2011-12-28 | 2011-12-28 | Absorbing tower with liquid self-flowing and stirring |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102489138A true CN102489138A (en) | 2012-06-13 |
Family
ID=46181023
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011104456077A Pending CN102489138A (en) | 2011-12-28 | 2011-12-28 | Absorbing tower with liquid self-flowing and stirring |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102489138A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105107626A (en) * | 2015-08-10 | 2015-12-02 | 自贡红星高压电瓷有限公司 | Real-time stirring and deironing process for high-iron rod insulator glaze slip |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2177519Y (en) * | 1992-11-02 | 1994-09-21 | 张学文 | Hydraulic stirrer |
| CN2206145Y (en) * | 1994-05-29 | 1995-08-30 | 钱建达 | Liquid material stirrer |
| WO2004071830A2 (en) * | 2003-02-11 | 2004-08-26 | The Boc Group, Inc. | Self-mixing tank |
| CN201410366Y (en) * | 2009-03-06 | 2010-02-24 | 浙江凯喜姆机械工业有限公司 | Blade-free stirred vessel |
| CN201529503U (en) * | 2009-10-13 | 2010-07-21 | 中芯国际集成电路制造(上海)有限公司 | Reaction pot mixing agitator |
| CN102120154A (en) * | 2010-01-11 | 2011-07-13 | 贵阳铝镁设计研究院 | Stirring method of multi-phase mixed liquid and conveying pipeline connecting structure adopted by same |
| CN202803087U (en) * | 2011-12-28 | 2013-03-20 | 云南氟业化工股份有限公司 | Absorption tower with liquid artesian flow stirring function |
-
2011
- 2011-12-28 CN CN2011104456077A patent/CN102489138A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2177519Y (en) * | 1992-11-02 | 1994-09-21 | 张学文 | Hydraulic stirrer |
| CN2206145Y (en) * | 1994-05-29 | 1995-08-30 | 钱建达 | Liquid material stirrer |
| WO2004071830A2 (en) * | 2003-02-11 | 2004-08-26 | The Boc Group, Inc. | Self-mixing tank |
| CN201410366Y (en) * | 2009-03-06 | 2010-02-24 | 浙江凯喜姆机械工业有限公司 | Blade-free stirred vessel |
| CN201529503U (en) * | 2009-10-13 | 2010-07-21 | 中芯国际集成电路制造(上海)有限公司 | Reaction pot mixing agitator |
| CN102120154A (en) * | 2010-01-11 | 2011-07-13 | 贵阳铝镁设计研究院 | Stirring method of multi-phase mixed liquid and conveying pipeline connecting structure adopted by same |
| CN202803087U (en) * | 2011-12-28 | 2013-03-20 | 云南氟业化工股份有限公司 | Absorption tower with liquid artesian flow stirring function |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105107626A (en) * | 2015-08-10 | 2015-12-02 | 自贡红星高压电瓷有限公司 | Real-time stirring and deironing process for high-iron rod insulator glaze slip |
| CN105107626B (en) * | 2015-08-10 | 2017-09-01 | 自贡红星高压电瓷有限公司 | The real-time stirring deferrization process of high ferro rod insulator glaze slip |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20120613 |