CN203139691U - Light/heavy phase material separation device - Google Patents
Light/heavy phase material separation device Download PDFInfo
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- CN203139691U CN203139691U CN 201320151867 CN201320151867U CN203139691U CN 203139691 U CN203139691 U CN 203139691U CN 201320151867 CN201320151867 CN 201320151867 CN 201320151867 U CN201320151867 U CN 201320151867U CN 203139691 U CN203139691 U CN 203139691U
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- separator
- liquid level
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- heavy phase
- phase outlet
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Abstract
The utility model discloses a light/heavy phase material separation device which comprises a separator, wherein a light phase outlet is formed above the separator; a heavy phase outlet is formed in the bottom of the separator; a liquid level meter is connected to the side wall of the separator; a mixing solution inlet is formed between the light phase outlet and the heavy phase outlet; an air outlet is further formed in the top of the separator; the air outlet is positioned above the light phase outlet; and the heavy phase outlet is connected with a valve or a liquid sealing pipeline. According to the provided light/heavy phase material separation device, continuous production operation can be realized without need of interrupting normal operation of a chemical reaction, the layered liquid level can be monitored at any time through a glass tube of the liquid level meter connected to the side wall, and materials or water with high specific gravity are discharged at any time, so that continuous and stable operation of the chemical reaction is realized, and various bad reactions caused by excessive materials with high specific gravity due to human factors are reduced to the greatest extent.
Description
Technical field
The utility model relates to a kind of weight phase materials separator, mainly is applicable to the feed separation technical field that proportion is different, for example technical field such as the separation of the separation of industrial chemicals and water, oil and water and the interruption between the industrial chemicals or continuous separation.
Background technology
The general method that adopts of the separation of emulsion material is in the prior art, the employing material leaves standstill a period of time in container after, manually separates again, generally need leave standstill the long period, and hold facility rate height.Artificial separation of the prior art need be interrupted to be carried out, and can not satisfy the requirement of production technology in continuity is produced, and needs operator's carefulness to observe, waste a large amount of time, cause loss of material easily, exist the separation equipment investment bigger simultaneously, cost is than problems such as height.
The utility model content
At problems of the prior art, particular problem to be solved in the utility model provides a kind of weight phase materials separator, can not need to interrupt normally carrying out of chemical reaction by this separator, directly carry out feed separation, and then satisfy the needs of successive reaction in the industrial production.
The utility model proposes a kind of weight phase materials separator, comprise separator, the top of described separator is provided with light phase export, the bottom of described separator is provided with heavy out, be connected with liquid level gauge on the sidewall of described separator, be provided with the mixed liquor import between described light phase export and the heavy out.
The top of described separator also is provided with exhaust outlet, and described exhaust outlet is positioned at the top of described light phase export.
Be connected by last interface, lower interface between described separator and the liquid level gauge, and described mixed liquor import is in described going up between interface and the lower interface.
Described mixed liquor import and described liquid level gauge relatively are arranged at the both sides of separator.
Described heavy out is connected with valve.
Described heavy out is connected with the fluid-tight pipeline.
The advantage that the utlity model has is:
The utility model provides a kind of weight phase materials separator, do not need to interrupt normally carrying out of chemical reaction, can continuous operation, the glass tube of the liquid level gauge that connects by sidewall can be monitored the layering liquid level at any time, at any time emit the bigger material of proportion or water, thereby make the carrying out of chemical reaction continous-stable, reduce because the artificial origin causes the too many various bad reactions that cause of anharmonic ratio heavy material as far as possible.
Description of drawings
Fig. 1 is the structural representation that the utility model provides a kind of weight phase materials separator.
Among the figure: the 1-separator; The 2-exhaust outlet; The 3-light phase export; The last interface of 4-; The 5-lower interface; The 6-heavy out; The import of 7-mixed liquor; 8-fluid-tight pipeline.
The specific embodiment
The utility model is described in further detail below in conjunction with the drawings and specific embodiments, so that those skilled in the art can better understand the utility model and being implemented, but illustrated embodiment is not as to restriction of the present utility model.
The utility model provides a kind of weight phase materials separator, as shown in Figure 1, comprise separator 1, the top of this separator 1 has light phase export 3, the bottom of this separator 1 has heavy out 6, also be connected with liquid level gauge on described separator 1 sidewall, this liquid level gauge is by being connected between last interface 4 and lower interface 5 and the separator 1, be provided with mixed liquor import 7 between described light phase export 3 and the heavy out 6, and the height of this mixed liquor import 7 is between the height of last interface 4 that liquid level gauge connects and lower interface 5, and be relatively arranged on the relative outer wall of separator 1 with liquid level gauge, the top of described light phase export 3 also is provided with exhaust outlet 2.Described heavy out 6 is connected with valve, opens this valve, the heavy phase after separating directly can be flowed out through this valve, and can adjust the height of the laminated fluid level in the separator 1 by the open degree of adjusting this valve.Heavy out 6 also can be connected with fluid-tight pipeline 8, can adjust the height that divides liquid layer in the separator 1 by the height of adjusting fluid-tight pipeline 8, and can also be provided with a valve between heavy out 6 and fluid-tight pipeline 8, is convenient to control.The emulsion material is from mixed liquor import 7 chargings of centre, along with the light phase materials in top is on the increase, flows out when arriving certain liquid level, and the anharmonic ratio heavy material builds up, treat the layering liquid level reach certain scale after automatic or manual separate.Material layering interface in the separator can directly be observed at the glass tube of liquid level gauge.The height of heavy phase and the layering interfaces of light phase can be by the heavy out place the open degree of valve carry out manual adjustments or the highly automated control by adjusting fluid-tight pipeline 8 at the relative fixed height and position.
The above embodiment is the preferred embodiment that proves absolutely that the utility model is lifted, and protection domain of the present utility model is not limited thereto.Being equal to that those skilled in the art do on the utility model basis substitutes or conversion, all within protection domain of the present utility model.Protection domain of the present utility model is as the criterion with claims.
Claims (6)
1. weight phase materials separator, it is characterized in that: comprise separator, the top of described separator is provided with light phase export, the bottom of described separator is provided with heavy out, be connected with liquid level gauge on the sidewall of described separator, be provided with the mixed liquor import between described light phase export and the heavy out.
2. weight phase materials separator according to claim 1, it is characterized in that: the top of described separator also is provided with exhaust outlet, and described exhaust outlet is positioned at the top of described light phase export.
3. weight phase materials separator according to claim 2 is characterized in that: be connected by last interface, lower interface between described separator and the liquid level gauge, and described mixed liquor import is in described going up between interface and the lower interface.
4. weight phase materials separator according to claim 3, it is characterized in that: described mixed liquor import and described liquid level gauge relatively are arranged at the both sides of separator.
5. weight phase materials separator according to claim 2, it is characterized in that: described heavy out is connected with valve.
6. weight phase materials separator according to claim 2, it is characterized in that: described heavy out is connected with the fluid-tight pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320151867 CN203139691U (en) | 2013-03-29 | 2013-03-29 | Light/heavy phase material separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320151867 CN203139691U (en) | 2013-03-29 | 2013-03-29 | Light/heavy phase material separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203139691U true CN203139691U (en) | 2013-08-21 |
Family
ID=48967248
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320151867 Expired - Fee Related CN203139691U (en) | 2013-03-29 | 2013-03-29 | Light/heavy phase material separation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203139691U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104892680A (en) * | 2015-06-08 | 2015-09-09 | 宁波大学 | Device for producing phosphorescent pyrimidine iridium complex |
| CN105289046A (en) * | 2015-10-23 | 2016-02-03 | 上海毅知实业有限公司 | Liquid separation device |
| CN108245915A (en) * | 2018-04-08 | 2018-07-06 | 江苏凌云药业股份有限公司 | A kind of azeotropic distillation separator |
| CN108745253A (en) * | 2018-08-02 | 2018-11-06 | 潍坊奥通药业有限公司 | The matching used automatic continuous mixing of continuous reaction device and Liquid liquid Separation device and method |
-
2013
- 2013-03-29 CN CN 201320151867 patent/CN203139691U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104892680A (en) * | 2015-06-08 | 2015-09-09 | 宁波大学 | Device for producing phosphorescent pyrimidine iridium complex |
| CN104892680B (en) * | 2015-06-08 | 2018-01-05 | 宁波大学 | Phosphorescence pyrimidine complex of iridium process units |
| CN105289046A (en) * | 2015-10-23 | 2016-02-03 | 上海毅知实业有限公司 | Liquid separation device |
| CN108245915A (en) * | 2018-04-08 | 2018-07-06 | 江苏凌云药业股份有限公司 | A kind of azeotropic distillation separator |
| CN108745253A (en) * | 2018-08-02 | 2018-11-06 | 潍坊奥通药业有限公司 | The matching used automatic continuous mixing of continuous reaction device and Liquid liquid Separation device and method |
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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: 20130821 Termination date: 20200329 |
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| CF01 | Termination of patent right due to non-payment of annual fee |