CN2394707Y - Mulilayer centrifugal liquid-gas reactor - Google Patents
Mulilayer centrifugal liquid-gas reactor Download PDFInfo
- Publication number
- CN2394707Y CN2394707Y CN 99239110 CN99239110U CN2394707Y CN 2394707 Y CN2394707 Y CN 2394707Y CN 99239110 CN99239110 CN 99239110 CN 99239110 U CN99239110 U CN 99239110U CN 2394707 Y CN2394707 Y CN 2394707Y
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- CN
- China
- Prior art keywords
- liquid
- gas
- container
- centrifugal
- disc
- 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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- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model relates to a multilayer centrifugal liquid-gas reactor. The liquid flowing into a container are splashed into the bead mist shape by the centrifugal principle by making use of a set of high-speed rotating discs to enlarge the contacting surface area of the liquid and the gas. The liquid are carried out the multilayer and repeated centrifugal splash, the liquid-gas reaction flow is long, and therefore, the liquid-gas reaction efficiency is enhanced.
Description
The utility model relates to a kind of liquid solid/liquid/gas reactions device, the centrifugal liquid solid/liquid/gas reactions of especially a kind of multilayer device.
At present, known liquid solid/liquid/gas reactions device generally is to make liquids and gases be contained in the interior flowing reactive of container of filler, and having weak point is that liquid and gas contact surface are long-pending little, so reaction efficiency is low.
It is long-pending that the purpose of this utility model provides a kind of centrifugal principle raising liquid gas contact surface that utilizes, and increase liquid gas contact flow process to improve the centrifugal liquid solid/liquid/gas reactions of the multilayer device of liquid solid/liquid/gas reactions efficient.
The purpose of this utility model is achieved in that the video disc that has a group to rotate at a high speed in container, this organizes video disc, between video disc and video disc, is separated by with the separator disc that has endoporus, and separator disc and container fuse; When liquid enters container when separator disc flow to video disc, the video disc of rotation relies on centrifugal force to make liquid to sputter all around at a high speed, the liquid of sputter becomes pearl vaporific, liquid after splashing down compiles by second layer separator disc and flow to second layer video disc, and rely on centrifugal principle to become pearl vaporific to sputter all around liquid once more, the liquid that splashes down continues to continue sputter by the separator disc downward one deck video disc that confluxes, flow to last one deck video disc until liquid and make the liquid that flows in the container become pearl vaporific, the gas in the container is the liquid haptoreaction vaporific with pearl.
Owing to adopt such scheme, utilize centrifugal principle to make the liquid bead in the container vaporific, liquid and gas contact surface in this state are long-pending big, and carry out centrifugal sputter repeatedly through multilayer, and liquid gas haptoreaction long flow path effectively improves liquid solid/liquid/gas reactions efficient.
Below in conjunction with drawings and Examples, the utility model is further specified.
The centrifugal liquid solid/liquid/gas reactions of figure one multilayer apparatus structure schematic diagram.
1 container, 2 inlets, 3 separator discs, 4 separator disc endoporus among the figure
5 liquid outlets, 6 air inlets, 7 video discs, 8 gas outlets
9 rotating shafts
In figure one, in container (1), fixedly mounting several layers video disc (7) in the rotating shaft (9), between every layer of video disc (7), there is separator disc (3) to separate, separator disc (3) center has through hole (4) to be installed in the container (1).Upper and lower side at container (1) has inlet (2) liquid outlet (5) air inlet (6) gas outlet (8), when liquid when inlet (2) enters container (1), when flowing to ground floor video disc (7) along ground floor separator disc (3) from separator disc, because video disc (7) is rotation at a high speed, liquid centrifugalization power is to sputter all around, making at ground floor becomes pearl vaporific with liquid between the second layer separator disc, liquid after splashing down confluxes to second layer video disc (7) along second layer separator disc (3), repeat above-mentioned sputter procedure, liquid splashes down the sputter of one deck video disc once, finishes until last one deck video disc sputter.Make the liquid between the interior every layer of separator disc of container become pearl vaporific entirely, in this state, liquid and gas can obtain sufficient haptoreaction.
Claims (1)
1 one kinds of liquid solid/liquid/gas reactions devices that video disc, rotating shaft, separator disc, container are formed, it is characterized in that: in the rotating shaft (9) in container (1), be installed with some video discs (7), between every layer of video disc (7), there is separator disc (3) to be separated by, there is through hole (4) at separator disc (3) center, and separator disc (3) is installed in the container (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 99239110 CN2394707Y (en) | 1999-07-28 | 1999-07-28 | Mulilayer centrifugal liquid-gas reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 99239110 CN2394707Y (en) | 1999-07-28 | 1999-07-28 | Mulilayer centrifugal liquid-gas reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2394707Y true CN2394707Y (en) | 2000-09-06 |
Family
ID=34026424
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 99239110 Expired - Fee Related CN2394707Y (en) | 1999-07-28 | 1999-07-28 | Mulilayer centrifugal liquid-gas reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2394707Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101745292B (en) * | 2008-12-16 | 2012-12-05 | 上海吴泾化工有限公司 | Multilevel open type turbine rotary disc agitated column for ketene continuous absorption and application thereof |
-
1999
- 1999-07-28 CN CN 99239110 patent/CN2394707Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101745292B (en) * | 2008-12-16 | 2012-12-05 | 上海吴泾化工有限公司 | Multilevel open type turbine rotary disc agitated column for ketene continuous absorption and application thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |