CN202460190U - Secondary diacolation extracting device - Google Patents
Secondary diacolation extracting device Download PDFInfo
- Publication number
- CN202460190U CN202460190U CN2012200992234U CN201220099223U CN202460190U CN 202460190 U CN202460190 U CN 202460190U CN 2012200992234 U CN2012200992234 U CN 2012200992234U CN 201220099223 U CN201220099223 U CN 201220099223U CN 202460190 U CN202460190 U CN 202460190U
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- pipeline
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- liquid outlet
- diacolation
- pump
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Abstract
The utility model discloses a secondary diacolation extracting device. A condenser (4), diacolation tanks (1) and (2), a cooler (5), a new solvent storage tank (7), a pump I (8), a heat exchanger (6), a pump III (10) and a liquid medicine storage tank (3) are respectively communicated with a valve through a pipeline. With the adoption of the secondary diacolation extracting device, an extracting liquid with low concentration is fully adopted, so that the using amount of a turnover solvent is greatly reduced, the concentration of the extracting liquid is increased, the energy consumption and the quantity of concentrated liquid are reduced, and the consumption loss of the solvent is reduced at the same time.
Description
Technical field
The utility model relates to a kind of secondary percolating extractor.
Background technology
Diacolation is extracted in extensive use in the effective ingredients in plant separation.It generally all is to adopt the one-level diacolation that present diacolation extracts, and its shortcoming is to extract continuously, causes that the solvent consume is big, energy consumption is big.
The utility model content
To the deficiency that prior art exists, the purpose of the utility model is to provide a kind of can fully apply mechanically the low concentration extract, improve extraction concentration, reduces the secondary percolating extractor that concentrates energy consumption and quantity, reduces the solvent consume.
The purpose of the utility model is to realize like this; The inlet of condenser is connected with the evacuation port of two diacolation tank tops through pipeline; The liquid outlet of condenser is connected with the inlet of cooler through pipeline, and the liquid outlet of cooler is connected with the inlet of novel solvent tank top through pipeline, and the liquid outlet of novel solvent tank bottom is connected on the inlet of pump I through pipeline; The liquid outlet of pump I is connected to the inlet of heat exchanger bottom through pipeline; With pipeline that heat exchanger top liquid outlet is connected on a threeway is installed, forms two pipelines, respectively install a valve h and i additional on the pipeline after separating; Article two, pipeline is connected with the inlet of two diacolation jars respectively, and at the inlet place valve c and e is installed respectively; The liquid outlet of a diacolation pot bottom is connected with the inlet of pump III through pipeline; Mounted valve g on the pipeline; The liquid outlet of pump III is connected with the inlet of soup storage tank through pipeline; Mounted valve a on the pipeline is communicated with the pipeline at No. two diacolation jar inlet places with the pipeline of a pipeline with pump III liquid outlet place, and on pipeline mounted valve f; The liquid outlet of No. two diacolation pot bottoms is connected with the inlet of pump II through pipeline; Mounted valve j on the pipeline; The liquid outlet of pump II is connected with the inlet of soup storage tank through pipeline; Mounted valve b on the pipeline is communicated with the pipeline at No. two diacolation jar inlet places with the pipeline of a pipeline with pump II liquid outlet place, and on pipeline mounted valve d.
The beneficial effect of the utility model is, adopts the utility model structure can the low concentration extract fully be applied mechanically, and reduces turnover solvent use amount greatly, improves extract concentration, reduces the energy consumption and the quantity that concentrate, reduces the consume of solvent simultaneously.
Description of drawings
Below in conjunction with accompanying drawing and embodiment the utility model is described further.
Accompanying drawing 1 is the structural representation of the utility model.
The specific embodiment
As shown in Figure 1; The utility model is that the inlet of condenser 4 is connected with the evacuation port at two diacolation jars 1 and 2 tops through pipeline; The liquid outlet of condenser 4 is connected with the inlet of cooler 5 through pipeline, and the liquid outlet of cooler 5 is connected with the inlet at novel solvent storage tank 7 tops through pipeline, and the liquid outlet of novel solvent storage tank 7 bottoms is connected on the inlet of pump I 8 through pipeline; The liquid outlet of pump I 8 is connected to the inlet of heat exchanger 6 bottoms through pipeline; With pipeline that heat exchanger 6 top liquid outlets are connected on a threeway is installed, forms two pipelines, respectively install a valve h and i additional on the pipeline after separating; Article two, pipeline is connected with 2 inlet with two diacolation jars 1 respectively, and at the inlet place valve c and e is installed respectively; The liquid outlet of diacolation jar 1 bottom is connected with the inlet of pump III 10 through pipeline; Mounted valve g on the pipeline; The liquid outlet of pump III 10 is connected with the inlet of soup storage tank 3 through pipeline; Mounted valve a on the pipeline is communicated with the pipeline at No. two diacolation jar 2 inlet places with the pipeline of a pipeline with pump III 10 liquid outlet places, and on pipeline mounted valve f; The liquid outlet of No. two diacolation jar 2 bottoms is connected with the inlet of pump II 9 through pipeline; Mounted valve j on the pipeline; The liquid outlet of pump II 9 is connected with the inlet of soup storage tank 3 through pipeline; Mounted valve b on the pipeline is communicated with the pipeline at No. two diacolation jar inlet places with the pipeline of a pipeline with pump II 9 liquid outlet places, and on pipeline mounted valve d.
With qinghaosu production is example, and artemisia leaf 1T is dropped into 5m
3In the diacolation jar; Benzinum injects the novel solvent storage tank, and benzinum passes through heat exchanger continuously with the speed of 1500L/H flow and is preheating to 60 ℃ through the pump of novel solvent storage tank bottom; Inject No. one extractor; Treat that liquid level reaches the liquid level indicated altitude, open diacolation pot bottom fluid valve No. one, percolate is injected the soup storage tank through pump.Behind the 7h, fluid is changed over to the 5m that installs the 1T artemisia leaf
3No. two diacolation jars, same, treat that liquid level reaches the liquid level indicated altitude, open diacolation pot bottom fluid valve No. two, through pump percolate is injected the soup storage tank.After treating that a percolate moves 10h, close the pump under the novel solvent storage tank, stop feed liquor.Diacolation jar continues fluid, to fully, closes diacolation pot bottom liquid valve and pump, simultaneously; Start the novel solvent system, benzinum is directly pumped into the diacolation jar No. two, simultaneously; No. one the diacolation jar begins straight-through Steam Recovery solvent 1h after bottom valve is closed, and deslagging advances the new raw material operation.After No. two the diacolation jar moves 7h equally, fluid is changed over to the 5m that installs the 1T artemisia leaf
3No. two diacolation jars, same, treat that liquid level reaches the liquid level indicated altitude, open diacolation pot bottom fluid valve No. one, through pump percolate is injected the soup storage tank.Circulation extraction operation so continuously.
Claims (1)
1. secondary percolating extractor; It is characterized in that: the inlet of condenser (4) is connected with the evacuation port of two diacolation jars (1) with (2) top through pipeline; The liquid outlet of condenser (4) is connected with the inlet of cooler (5) through pipeline, and the liquid outlet of cooler (5) is connected with the inlet at novel solvent storage tank (7) top through pipeline, and the liquid outlet of novel solvent storage tank (7) bottom is connected on the inlet of pump I (8) through pipeline; The liquid outlet of pump I (8) is connected to the inlet of heat exchanger (6) bottom through pipeline; With pipeline that heat exchanger (6) top liquid outlet is connected on a threeway is installed, forms two pipelines, respectively install a valve h and i additional on the pipeline after separating; Article two, pipeline is connected with the inlet of two diacolation jars (1) and (2) respectively, and at the inlet place valve c and e is installed respectively; The liquid outlet of a diacolation jar (1) bottom is connected with the inlet of pump III (10) through pipeline; Mounted valve g on the pipeline; The liquid outlet of pump III (10) is connected with the inlet of soup storage tank (3) through pipeline; Mounted valve a on the pipeline is communicated with the pipeline at No. two diacolation jars (2) inlet place with the pipeline of a pipeline with pump III (10) liquid outlet place, and on pipeline mounted valve f; The liquid outlet of No. two diacolation jars (2) bottom is connected with the inlet of pump II (9) through pipeline; Mounted valve j on the pipeline; The liquid outlet of pump II (9) is connected with the inlet of soup storage tank (3) through pipeline; Mounted valve b on the pipeline is communicated with the pipeline at No. two diacolation jar inlet places with the pipeline of a pipeline with pump II (9) liquid outlet place, and on pipeline mounted valve d.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200992234U CN202460190U (en) | 2012-03-08 | 2012-03-08 | Secondary diacolation extracting device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200992234U CN202460190U (en) | 2012-03-08 | 2012-03-08 | Secondary diacolation extracting device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202460190U true CN202460190U (en) | 2012-10-03 |
Family
ID=46908391
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012200992234U Expired - Lifetime CN202460190U (en) | 2012-03-08 | 2012-03-08 | Secondary diacolation extracting device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202460190U (en) |
-
2012
- 2012-03-08 CN CN2012200992234U patent/CN202460190U/en not_active Expired - Lifetime
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20121003 |
|
| CX01 | Expiry of patent term |