CN203043617U - Percolation tank - Google Patents
Percolation tank Download PDFInfo
- Publication number
- CN203043617U CN203043617U CN 201320051993 CN201320051993U CN203043617U CN 203043617 U CN203043617 U CN 203043617U CN 201320051993 CN201320051993 CN 201320051993 CN 201320051993 U CN201320051993 U CN 201320051993U CN 203043617 U CN203043617 U CN 203043617U
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- CN
- China
- Prior art keywords
- tank body
- upper tank
- extract
- end socket
- utility
- 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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Abstract
The utility model discloses a percolation tank. The percolation tank comprises a tank body, wherein the tank body comprises an upper tank body and a lower tank body; the lower tank body is connected with a seal head via a flange; a filter plate is arranged on the seal head; a discharge hole is formed at the bottom end of the seal head; a feeding hole is formed at the top of the upper tank body; at least a liquid inlet is formed on the feeding hole; at least two supports are also arranged on the upper tank body; and the upper tank body is also provided with a window, a pressure meter and a thermometer. The percolation tank can achieve continuous extraction of natural plants and reach a high extraction ratio.
Description
Technical field
The utility model relates to a kind of extraction equipment, especially a kind of diacolation jar.
Background technology
At present in the extracted form natural plant industry, it is comparatively general that extractor is used, reason is that extractor is made simply, even if reactor, also can be used for extracting the active ingredient in the plant after making improvements slightly, but there is the shortcoming that recovery rate is low, can not continous way extract usually in existing extractor.
As everyone knows, the active ingredient that extractor extracts natural plants generally all is to adopt intermittent operation, the material that is about to need to extract is put into jar, add extract again and leave standstill a period of time, then extract is extracted out with pump, in the process that leaves standstill, because the active ingredient in the material precipitate in the extract, cause the active constituent content in the extract to raise gradually, and the concentration of active ingredient is more high in the extract, material is separated out the speed of active ingredient will be more and more slower, thereby cause the extracts active ingredients of material incomplete, and another shortcoming of using extractor to extract is, has only and extract could be extracted out after extract and material left standstill a period of time, then carry out the extraction operation of next group again, therefore can't realize the extraction operation of continous way.
The utility model content
The utility model is at the deficiencies in the prior art, and purpose is to provide a kind of diacolation jar, can realize enough that the continous way of natural plants is extracted and higher recovery rate.
The utility model realizes that the technical scheme of above-mentioned purpose is: a kind of diacolation jar, comprise tank body, tank body is made up of upper tank body and lower tank, described lower tank is connected with end socket by flange, and described end socket is provided with filter plate, and described end socket bottom is provided with discharging opening, described upper tank body top is provided with dog-house, described dog-house is provided with at least one inlet, also is provided with at least two supports on the upper tank body, also is provided with form, pressure gauge and thermometer on the upper tank body.
The aspect ratio of described upper tank body and lower tank is 1:1 ~ 1:3.
Described upper tank body is cylindrical, and described lower tank is conical.
The aperture of described filter plate is 100 ~ 400 orders.
The beneficial effects of the utility model are: the utility model is by after joining material in the tank body, from inlet extract is imported continuously, extract with active ingredient is precipitate in the extract after material contacts fully, and continue to flow out from discharging opening, the content of active ingredient in extract can be more and more lower in the whole leaching process, thereby the active ingredient in the material is better precipitate in the extract, not only realize the charging and discharging of continous way, also realized the effect of high extraction.
Description of drawings
Fig. 1 is structural representation of the present utility model;
Fig. 2 is vertical view of the present utility model.
Among the figure: flange 1, lower tank 2, upper tank body 3, end socket 4, dog-house 5, support 6, form 7, pressure gauge 8, thermometer 9, tank body 10, filter plate 41, discharging opening 42, inlet 51.
The specific embodiment
Below in conjunction with accompanying drawing, and in conjunction with the embodiments, the utility model is described further.
Embodiment 1:
As shown in Figure 1 and Figure 2, a kind of diacolation jar, comprise tank body 10, tank body 10 is made up of upper tank body 3 and lower tank 2, and described lower tank 2 is connected with end socket 4 by flange 1, described end socket 4 is provided with filter plate 41, described end socket 4 bottoms are provided with discharging opening 42, and described upper tank body 3 tops are provided with dog-house 5, and described dog-house 5 is provided with at least one inlet 51, also be provided with at least two supports 6 on the upper tank body 3, also be provided with form 7, pressure gauge 8 and thermometer 9 on the upper tank body 3.
The aspect ratio of described upper tank body 3 and lower tank 2 is 1:1 ~ 1:3.
Described upper tank body 3 is cylindrical, and described lower tank 2 is conical.
The aperture of described filter plate 41 is 100 ~ 400 orders.
The course of work of the present utility model is: material can be put into the tank body 10 from dog-house 5, the height of material generally is no more than 2/3rds of tank body 10 height, extract enters into tank body 10 from inlet 51, contacting the back fully with material flows out from discharging opening 42, in the process of contact, active ingredient in the material is precipitate in the extract, because extract is continuous flow regime, thereby content of effective can be more and more lower in the extract in whole process, further accelerate the speed of separating out of the active ingredient in the material, after finishing the extraction operation, opened flange 1, lay down end socket 4, material is discharged from the bottom of diacolation jar.
The support 6 of the utility model setting makes things convenient for installation and the location of diacolation jar, and the design of form 7, pressure gauge 8 and thermometer 9 then can allow the operator observe liquid level, the pressure and temperature of tank body 10 easily.
Claims (4)
1. diacolation jar, it is characterized in that: comprise tank body (10), tank body (10) is made up of upper tank body (3) and lower tank (2), described lower tank (2) is connected with end socket (4) by flange (1), described end socket (4) is provided with filter plate (41), described end socket (4) bottom is provided with discharging opening (42), described upper tank body (3) top is provided with dog-house (5), described dog-house (5) is provided with at least one inlet (51), also be provided with at least two supports (6) on the upper tank body (3), also be provided with form (7) on the upper tank body (3), pressure gauge (8) and thermometer (9).
2. diacolation jar as claimed in claim 1, it is characterized in that: the aspect ratio of described upper tank body (3) and lower tank (2) is 1:1 ~ 1:3.
3. diacolation jar as claimed in claim 1 is characterized in that: described upper tank body (3) is for cylindrical, and described lower tank (2) be taper shape.
4. diacolation jar as claimed in claim 1, it is characterized in that: the aperture of described filter plate (41) is 100 ~ 400 orders.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320051993 CN203043617U (en) | 2013-01-30 | 2013-01-30 | Percolation tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320051993 CN203043617U (en) | 2013-01-30 | 2013-01-30 | Percolation tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203043617U true CN203043617U (en) | 2013-07-10 |
Family
ID=48726618
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320051993 Expired - Fee Related CN203043617U (en) | 2013-01-30 | 2013-01-30 | Percolation tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203043617U (en) |
-
2013
- 2013-01-30 CN CN 201320051993 patent/CN203043617U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130710 Termination date: 20140130 |