CN201101961Y - Gas-liquid-solid mixing reactor - Google Patents
Gas-liquid-solid mixing reactor Download PDFInfo
- Publication number
- CN201101961Y CN201101961Y CNU2007201846747U CN200720184674U CN201101961Y CN 201101961 Y CN201101961 Y CN 201101961Y CN U2007201846747 U CNU2007201846747 U CN U2007201846747U CN 200720184674 U CN200720184674 U CN 200720184674U CN 201101961 Y CN201101961 Y CN 201101961Y
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- CN
- China
- Prior art keywords
- gas
- liquid
- air distribution
- distribution disk
- solid
- 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.)
- Expired - Fee Related
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- Mixers Of The Rotary Stirring Type (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model discloses a gas-liquid-solid stirred reactor which comprises an electrical motor 6, a hollow stirred shaft 1, a gas-distributing disc 4 and a stirred oar 5. A vent port 42 of the gas-distributing disc 4 is provided with an air flue arc plate 41 which protuberates from the circumference of the gas-distributing disc 4. A material inlet 7 is arranged on the gas-distributing disc 4. The gas-liquid-solid stirred reactor has the advantages of high stirring efficiency and easy gas-liquid-solid blend.
Description
Technical field
The utility model relates to the solid stirred reactor of a kind of gas-liquid, particularly a kind of air distribution disk of gas-liquid gas-solids reactors.
Background technology
The operation principle of the solid stirred reactor of gas-liquid is: gas liquid and solid in reactor, react, make gas liquid and solid in retort, fully mix, the motion of driven by motor shaft coupling, be connected with air distribution disk and paddle on the shaft coupling, come like this in the stirred reactor liquid gas and solid.Air distribution disk is in high speed rotating, because the row of pushing away material make and produced cavity around the air distribution disk, and the above gas pressure of liquid level is higher than air distribution disk pressure on every side, so the meeting of the gas on liquid level elder generation is by the through hole of shaft coupling, pass through hollow shaft again, shaft and air distribution disk gas outlet below arriving, again by air distribution disk gas dispersion to rotating because of dispersion impeller in the cavity produce, material also can be by the material inlet that has on the air distribution disk simultaneously, in the inflow air distribution disk, rotate to push away through air distribution disk again and be discharged in the cavity that produces because of the air distribution disk rotation, material and gas enter the cavity that produces because of the air distribution disk rotation simultaneously, solid is upwards dug under the high-revolving promotion of the blade of three leaf push types simultaneously, thereby gas is more contacted with the solid material surface with liquid.But existing air distribution disk is a disk, and the effect that produces air pressure and cavity is undesirable, and material only moves in retort, and stirring efficiency is not high.
Summary of the invention
Shortcoming at existing air distribution disk provides a kind of air distribution disk that improves the solid mixing efficiency of gas-liquid.
To achieve these goals, the measure that the utility model is taked is: the solid stirred reactor of a kind of gas-liquid comprises motor 6, hollow shaft 1, and air distribution disk 4 and paddle 5,42 places, gas outlet of air distribution disk 4 are provided with the air flue arc plate 41 that is projected on air distribution disk 4 circumference.Air distribution disk 4 is provided with material inlet 7, has gas outlet 42 under air flue.
The utility model has the advantages that: stirring efficiency height, gas-liquid mix admittedly easily.
Description of drawings
Fig. 1. structural representation of the present utility model.
Fig. 2. the structural representation of air distribution disk.
Fig. 3. the A-A of Fig. 2 is to view.
The figure number explanation
1...... hollow shaft 2......... air inlet
3...... bolt 4......... air distribution disk
5........ paddle 6....... motor
7........ material inlet 41...... air flue arc plate
42........ 421...... gas outlet, gas outlet
The specific embodiment
See also its implementation process of description of drawings: the solid stirred reactor of a kind of gas-liquid, comprise motor 6, hollow shaft 1, motor 6 drive hollow shaft 1 motion, are fixed with air distribution disk 4 and paddle 5 on the hollow shaft 1 respectively.The air flue arc plate 41 that is projected on air distribution disk 4 circumference is located to be provided with in the gas outlet 42 (421) of air distribution disk 4.The scope of 4 rows of pushing away materials generation cavity is bigger from 2 li gases that enter of air inlet from air distribution disk like this, the mixing of easier acceleration gas and liquid.Air distribution disk 4 is provided with material inlet 7, has gas outlet 42 (421) under air flue, and liquid also can enter air distribution disk 4 like this, makes liquid just begin to mix before gas ejection air distribution disk, and mixed effect is better.
Claims (2)
1, the solid stirred reactor of a kind of gas-liquid comprises motor (6), and hollow shaft (2), and air distribution disk (4) and paddle (5) is characterized in that the air flue arc plate (41) that is projected on air distribution disk (4) circumference is located to be provided with in the gas outlet (42) of air distribution disk (4).
2, the solid stirred reactor of a kind of gas-liquid according to claim 1 is characterized in that air distribution disk (4) is provided with material inlet (7), has gas outlet (42,421) under air flue.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201846747U CN201101961Y (en) | 2007-10-18 | 2007-10-18 | Gas-liquid-solid mixing reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201846747U CN201101961Y (en) | 2007-10-18 | 2007-10-18 | Gas-liquid-solid mixing reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201101961Y true CN201101961Y (en) | 2008-08-20 |
Family
ID=39948979
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007201846747U Expired - Fee Related CN201101961Y (en) | 2007-10-18 | 2007-10-18 | Gas-liquid-solid mixing reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201101961Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102847504A (en) * | 2012-08-29 | 2013-01-02 | 南通赛孚机械设备有限公司 | Stirring shaft in reaction vessel |
| CN102861548A (en) * | 2010-09-20 | 2013-01-09 | 浙江诚信医化设备有限公司 | Stirring type reacting kettle |
| CN104056585A (en) * | 2014-06-20 | 2014-09-24 | 景鹏飞 | Efficient solid-liquid stirring overflow reaction kettle |
| CN113842854A (en) * | 2021-08-24 | 2021-12-28 | 深圳市银宝山新科技股份有限公司 | Reaction device |
-
2007
- 2007-10-18 CN CNU2007201846747U patent/CN201101961Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102861548A (en) * | 2010-09-20 | 2013-01-09 | 浙江诚信医化设备有限公司 | Stirring type reacting kettle |
| CN102847504A (en) * | 2012-08-29 | 2013-01-02 | 南通赛孚机械设备有限公司 | Stirring shaft in reaction vessel |
| CN104056585A (en) * | 2014-06-20 | 2014-09-24 | 景鹏飞 | Efficient solid-liquid stirring overflow reaction kettle |
| CN104056585B (en) * | 2014-06-20 | 2016-03-16 | 闫军政 | High efficiency solid-liquid stirs overflow reactor |
| CN113842854A (en) * | 2021-08-24 | 2021-12-28 | 深圳市银宝山新科技股份有限公司 | Reaction device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080820 Termination date: 20151018 |
|
| EXPY | Termination of patent right or utility model |