CN203208721U - Continuous extraction device - Google Patents
Continuous extraction device Download PDFInfo
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- CN203208721U CN203208721U CN 201220631381 CN201220631381U CN203208721U CN 203208721 U CN203208721 U CN 203208721U CN 201220631381 CN201220631381 CN 201220631381 CN 201220631381 U CN201220631381 U CN 201220631381U CN 203208721 U CN203208721 U CN 203208721U
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- filter
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Abstract
The utility model discloses a continuous extraction device. The continuous extraction device comprises a first storage tank, wherein the first storage tank is connected with a No. 1 pump, the No. 1 pump is sequentially connected with a flow meter and a first valve, an outlet of the first valve is divided into two lines, one line is sequentially connected with a second valve, a first percolation tank and a third valve, the other line is sequentially connected with a fourth valve, a second percolation tank and a fifth valve, the outlets of the third valve and the fifth valve are converged and then connected with a heat exchanger, the heat exchanger is connected with a disk separation machine, the disk separation machine is connected with a No. 2 pump, and the No. 2 pump is connected with a second storage tank. The device disclosed by the utility model has lower cost, can realize continuous operation and is suitable for large-scale industrial extraction operation.
Description
Technical field
The utility model relates to a kind of continous way extraction element, is applied to the extraction of the active ingredient of natural plants.
Background technology
Natural plants and Chinese herbal medicine be by the increasing various fields such as medicine, food, spices that are used for, and is its important mode and link to the extraction of natural plant raw material active ingredient.Extraction to natural plants mainly is to adopt still formula heating lixiviate at present, and this mode extraction efficiency is not high, and the time is long, and energy consumption is big, can not realize continous way and large batch of operation.Number be the high-efficiency device for extracting of the extraction effective ingredients in plant of CN202044951U as Granted publication, raw material fragmentation, heating lixiviate, ultrasonic extraction be fused into as a whole, reduced intermediate link, saved extraction time, improved operating efficiency.But this extraction element is a kind of batch (-type) extraction element in fact still, still has the problem of an extracting cycle, is not easy to the continous way operation, and the equipment investment that the industrialization ultrasonic wave extracts is too big, and general enterprise is unable bears.
The utility model content
The utility model is at the deficiencies in the prior art, and purpose is to provide a kind of continous way extraction element, and this device can be realized the continous way extraction, and the cost of equipment is lower.
The utility model realizes that the technical scheme of above-mentioned purpose is: a kind of continous way extraction element, comprise first storage tank, first storage tank connects a pump, pump is connection traffic meter and first valve successively, the outlet of first valve is divided into two-way, one the tunnel connects second valve, the first diacolation jar and the 3rd valve successively, another road connects the 4th valve, the second diacolation jar and the 5th valve successively, after converging, the outlet of the 3rd valve and the 5th valve is connected heat exchanger, heat exchanger connects disc separator, disc separator connects No. two pumps, and No. two pump connects second storage tank.
The described first diacolation pot bottom is provided with first filter.
The described second diacolation pot bottom is provided with second filter.
The aperture of described first filter is 10 ~ 100 orders.
The aperture of described second filter is 10 ~ 100 orders.
The beneficial effects of the utility model are: installation cost of the present utility model is lower, and can realize the continous way operation, is fit to large-scale industrialization and extracts operation.
Description of drawings
Fig. 1 is structural representation of the present utility model.
Among the figure: first storage tank 1, pump 2, flowmeter 3, heat exchanger 4, disc separator 5, No. two pumps 6, second storage tank 7, first valve 11, second valve 12, the 3rd valve 13, the 4th valve 14, the 5th valve 15, the first diacolation jar 21, the second diacolation jar 22, first filter 212, second filter 222.
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, a kind of continous way extraction element, comprise first storage tank 1, first storage tank 1 connects a pump 2, pump 2 is connection traffic meter 3 and first valve 11 successively, the outlet of first valve 11 is divided into two-way, one the tunnel connects second valve 12, the first diacolation jar 21 and the 3rd valve 13 successively, another road connects the 4th valve 14, the second diacolation jar 22 and the 5th valve 15 successively, after converging, the outlet of the 3rd valve 13 and the 5th valve 15 is connected heat exchanger 4, heat exchanger 4 connects disc separator 5, and disc separator 5 connects 6, No. two pumps of No. two pumps 6 and connects second storage tank 7.
The described first diacolation jar 21 bottoms are provided with first filter 212.
The described second diacolation jar 22 bottoms are provided with second filter 222.
The aperture of described first filter 212 is 10 ~ 100 orders.
The aperture of described second filter 222 is 10 ~ 100 orders.
The course of work of the present utility model is: store extract in first storage tank 1, extract pumps through a pump 2, flow through flowmeter 3 and first valve 11, by regulating first valve, 11 adjustable throttle amounts, can control the flow direction of extract and (as open second valve 12 by regulating second valve 12 and the 4th valve 14, close 14 extracts of the 4th valve and flow to the first diacolation jar 21), the first diacolation jar 21 and the second diacolation jar 22 can switch mutually, that is to say after a diacolation jar is finished the extraction operation, switch to another diacolation jar, so can realize continual operation, the material that needs extraction is housed in the diacolation jar; The extract diacolation jar of flowing through, fully contact with material, active ingredient in the material is precipitate in the extract, after heat exchanger 4 heat exchange, flow into disc separator 5, in disc separator 5, realize Separation of Solid and Liquid, reach the effect of solid residue in the separation and Extraction liquid, the extract after Separation of Solid and Liquid is pumped into second storage tank 7 by No. two pumps 6 and stores.
The effect of first filter 212 and second filter 222 is that extract is carried out preliminary Separation of Solid and Liquid, to alleviate the operating pressure of disc separator 5.
Claims (1)
1. continous way extraction element, it is characterized in that: comprise first storage tank (1), first storage tank (1) connects a pump (2), a pump (2) is connection traffic meter (3) and first valve (11) successively, the outlet of first valve (11) is divided into two-way, one the tunnel connects second valve (12) successively, the first diacolation jar (21) and the 3rd valve (13), another road connects the 4th valve (14) successively, the second diacolation jar (22) and the 5th valve (15), after converging, the outlet of the 3rd valve (13) and the 5th valve (15) is connected heat exchanger (4), heat exchanger (4) connects disc separator (5), disc separator (5) connects No. two pumps (6), and No. two pumps (6) connect second storage tank (7); The described first diacolation jar (21) bottom is provided with first filter (212); The described second diacolation jar (22) bottom is provided with second filter (222); The aperture of described first filter (212) is 10 ~ 100 orders; The aperture of described second filter (222) is 10 ~ 100 orders.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220631381 CN203208721U (en) | 2012-11-25 | 2012-11-25 | Continuous extraction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220631381 CN203208721U (en) | 2012-11-25 | 2012-11-25 | Continuous extraction device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203208721U true CN203208721U (en) | 2013-09-25 |
Family
ID=49198295
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220631381 Expired - Fee Related CN203208721U (en) | 2012-11-25 | 2012-11-25 | Continuous extraction device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203208721U (en) |
-
2012
- 2012-11-25 CN CN 201220631381 patent/CN203208721U/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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130925 Termination date: 20151125 |