CN204734981U - High -efficient diacolation extraction element - Google Patents
High -efficient diacolation extraction element Download PDFInfo
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- CN204734981U CN204734981U CN201520454548.3U CN201520454548U CN204734981U CN 204734981 U CN204734981 U CN 204734981U CN 201520454548 U CN201520454548 U CN 201520454548U CN 204734981 U CN204734981 U CN 204734981U
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- cooler
- diacolation
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- vaporization chamber
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- 238000000605 extraction Methods 0.000 title claims abstract description 34
- 238000010438 heat treatment Methods 0.000 claims abstract description 19
- 239000002904 solvent Substances 0.000 claims description 29
- 238000009834 vaporization Methods 0.000 claims description 26
- 238000001914 filtration Methods 0.000 claims description 23
- 238000005325 percolation Methods 0.000 claims description 23
- 230000005484 gravity Effects 0.000 claims description 12
- 230000001502 supplementation Effects 0.000 claims description 7
- 238000001704 evaporation Methods 0.000 abstract description 4
- 230000000694 effects Effects 0.000 description 12
- 101700072563 POT1 Proteins 0.000 description 11
- 238000004891 communication Methods 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 239000012530 fluid Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 241001163443 Daphne giraldii Species 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 239000000284 extract Substances 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000012141 concentrate Substances 0.000 description 2
- 238000002386 leaching Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 241000934856 Daphne Species 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000002269 spontaneous Effects 0.000 description 1
Abstract
The utility model relates to a high -efficient diacolation extraction element belongs to the diacolation and draws equipment technical field, the technical problem that will solve provides a high efficiency diacolation extraction element that circulates and draw completely, in order to solve the technical problems, the utility model provides a high -efficient diacolation extraction element, includes that the diacolation draws jar, pair filter, heating chamber, evaporating chamber, condenser, six equipment in the cooler, six equipment pass through the whole that the pipe connection is an intercommunication according to the serial number in proper order, and wherein, the focus horizontal position that the diacolation drawed jar, condenser and cooler risees in proper order, and the focus horizontal position of evaporating chamber is higher than the heating chamber, and the focus horizontal position of cooler is higher than the evaporating chamber, the utility model discloses a leading features is exactly, the entrance point department that draws jar except the exit end of cooler or diacolation is provided with the flow control valve door, six equipment connecting tube and port of connecting tube between two liang does not set up other control flap.
Description
Technical field
A kind of efficient percolating extractor of the utility model, belongs to seepage pressure effects equipment technical field.
Background technology
The aseptic aqueous solution that Daphne giraldii Nitsche injection liquid makes after extraction purification for Chinese medicine girald daphne bark, its active ingredient is dephnetin composition.The extraction of current Daphne giraldii Nitsche injection liquid adopts, and for being joined in seepage pressure effects extractor by medicinal material, adding certain density ethanolic solution and carrying out seepage pressure effects, percolate flows in fluid reservoir, and transfer in inspissator and carry out heating reduced pressure concentration, operation is longer, need man-hour more, need equipment more.
Patent CN 203469533 U Chinese medicine continuous circumfluence extraction device relate to a kind of device that can realize refluxing extraction, after but this device still needs to complete extraction in use in extractor, just can open the discharge valve of extractor, extract and medicine enter follow-up equipment and concentrate.The extraction that circulates completely can not be realized.
Utility model content
The utility model overcomes the deficiencies in the prior art, and technical problem to be solved is to provide a kind of high efficiency percolating extractor that can realize real-time circulation and extract.
For solving the problems of the technologies described above, the technical scheme that the utility model adopts is: a kind of efficient percolating extractor, comprises percolation filtration extraction pot, duplex strainer, heating clamber, vaporization chamber, condenser, cooler six equipment;
The discharging opening of percolation filtration extraction pot is by the inlet communication of pipeline and duplex strainer; The liquid outlet of duplex strainer is communicated with the inlet of heating clamber by pipeline; Heating clamber is communicated with vaporization chamber by pipeline, and vaporization chamber is communicated with condenser by pipeline, and condenser is communicated with cooler by pipeline; Cooler is by the solvent inlet of pipeline communication percolation filtration extraction pot.The position relationship of described six equipment is: the horizontal location of the center of gravity of percolation filtration extraction pot, condenser and cooler raises successively, and the horizontal location of the center of gravity of vaporization chamber is higher than heating clamber, and the horizontal location of the center of gravity of cooler is higher than vaporization chamber.
A principal character of the present utility model is exactly, except the port of export of cooler or the solvent inlet end place of percolation filtration extraction pot are provided with except flow control valve, the port of described six equipment connecting pipe between any two and connecting pipe does not arrange other by-pass valve controls.
When above-mentioned structure makes to adopt the utility model to carry out seepage pressure effects to medicinal material, described six equipment are communicated with in leaching process always, solvent, the solvent carrying effective ingredient or solvent vapo(u)r in percolating extractor all the time not in reciprocation cycle.The hydraulic pressure etc. of the vapour pressure formed by vaporization chamber, negative pressure that cooler is formed, percolation filtration extraction pot, really achieves the integration of seepage pressure effects, the operation such as concentrated, has saved extraction time greatly, improve production efficiency.
This structure can ensure, in a diacolation process, no longer to need plus solvent.
In addition, can also arrange pressure detector at the steam outlet of vaporization chamber, described cooler also arranges solvent pair and adds mouth, and described solvent pair is added mouth and is used for the supplementing solvent when pressure detector detects insufficient pressure.Or arrange pressure detector at the steam outlet of vaporization chamber, described percolation filtration extraction pot also arranges solvent pair and adds mouth, and described solvent pair is added mouth and is used for the supplementing solvent when pressure detector detects insufficient pressure.
The design of above-mentioned two kinds of forms, be due to each seepage pressure effects complete after can opening can take away partial solvent except the dregs of a decoction, or also have other forms of loss, carry out again next time seepage pressure effects time, after percolating extractor forms circulation, by observing the force value of pressure detector, required pressure criteria value during beginning, can be less than, need to open solvent pair and add mouth supplementing solvent, until the force value of pressure detector reaches required pressure criteria value.
When adopting the utility model to carry out seepage pressure effects, after Inner eycle is stable, percolate directly puts into inspissator with constant speed, diacolation reduced pressure concentration, the steam that evaporation produces is condensed into water again and joins in seepage pressure effects device, realize limit seepage pressure effects, limit concentrates, and concentration and recovery water enters in seepage pressure effects device again.Saved the fluid reservoir that percolate is deposited, percolate is put into fluid reservoir from seepage pressure effects device, then operation fluid reservoir being put into inspissator becomes the operation directly percolate being put into inspissator, has saved a procedure, has shortened the working time of 4 hours.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, the utility model is described in further detail.
Fig. 1 is structural representation of the present utility model.
In figure: 1 is percolation filtration extraction pot, 2 is duplex strainer, and 3 is heating clamber, and 4 is vaporization chamber, and 5 is condenser, and 6 is cooler.
Detailed description of the invention
Below in conjunction with specific embodiment, the utility model is described in further detail.
Embodiment 1
A kind of efficient percolating extractor, comprises percolation filtration extraction pot 1, duplex strainer 2, heating clamber 3, vaporization chamber 4, condenser 5, cooler 6 six equipment;
The discharging opening of percolation filtration extraction pot 1 is by the inlet communication of pipeline and duplex strainer 2; The liquid outlet of duplex strainer 2 is communicated with by the inlet of pipeline with heating clamber 3; Heating clamber 3 is communicated with vaporization chamber 4 by pipeline, and vaporization chamber 4 is communicated with condenser 5 by pipeline, and condenser 5 is communicated with cooler 6 by pipeline; Cooler 6 is by the solvent inlet of pipeline communication percolation filtration extraction pot 1.The position relationship of described six equipment is: the horizontal location of the center of gravity of percolation filtration extraction pot 1, condenser 5 and cooler 6 raises successively, and the horizontal location of the center of gravity of vaporization chamber 4 is higher than heating clamber 3, and the horizontal location of the center of gravity of cooler 6 is higher than vaporization chamber 4.
Except the port of export of cooler 6 or the entrance point place of percolation filtration extraction pot 1 are provided with except flow control valve, the port of described six equipment connecting pipe between any two and connecting pipe does not arrange other by-pass valve controls.
In addition, arrange pressure detector at the steam outlet of vaporization chamber 4, described cooler 6 also arranges solvent pair and adds mouth, and described solvent pair is added mouth and is used for the supplementing solvent when pressure detector detects insufficient pressure.
Embodiment 2
A kind of efficient percolating extractor, comprises percolation filtration extraction pot 1, duplex strainer 2, heating clamber 3, vaporization chamber 4, condenser 5, cooler 6 six equipment;
The discharging opening of percolation filtration extraction pot 1 is by the inlet communication of pipeline and duplex strainer 2; The liquid outlet of duplex strainer 2 is communicated with by the inlet of pipeline with heating clamber 3; Heating clamber 3 is communicated with vaporization chamber 4 by pipeline, and vaporization chamber 4 is communicated with condenser 5 by pipeline, and condenser 5 is communicated with cooler 6 by pipeline; Cooler 6 is by the solvent inlet of pipeline communication percolation filtration extraction pot 1.The position relationship of described six equipment is: the horizontal location of the center of gravity of percolation filtration extraction pot 1, condenser 5 and cooler 6 raises successively, and the horizontal location of the center of gravity of vaporization chamber 4 is higher than heating clamber 3, and the horizontal location of the center of gravity of cooler 6 is higher than vaporization chamber 4.
Except the port of export of cooler 6 or the entrance point place of percolation filtration extraction pot 1 are provided with except flow control valve, the port of described six equipment connecting pipe between any two and connecting pipe does not arrange other by-pass valve controls.
In addition, arrange pressure detector at the steam outlet of vaporization chamber 4, described percolation filtration extraction pot 1 also arranges solvent pair and adds mouth, and described solvent pair is added mouth and is used for the supplementing solvent when pressure detector detects insufficient pressure.
By reference to the accompanying drawings embodiment of the present utility model is explained in detail above, but the utility model is not limited to above-described embodiment, in the ken that those of ordinary skill in the art possess, various change can also be made under the prerequisite not departing from the utility model aim.Such as, although the utility model extracts demand according to Daphne giraldii Nitsche injection liquid and develops, form spontaneous circulation in its leaching process inherently different from the medicinal material of other kinds to the requirement of caliber, but those skilled in the art can design the power of caliber or heating clamber according to actual needs.
Claims (3)
1. an efficient percolating extractor, is characterized in that: comprise percolation filtration extraction pot (1), duplex strainer (2), heating clamber (3), vaporization chamber (4), condenser (5), cooler (6) six equipment; It is the entirety be communicated with that described six equipment are connected by pipeline according to number order, especially only has the entrance point place of the port of export of cooler (6) or percolation filtration extraction pot (1) to be provided with flow control valve; Wherein, the horizontal location of the center of gravity of percolation filtration extraction pot (1), condenser (5) and cooler (6) raises successively, and the horizontal location of the center of gravity of vaporization chamber (4) is higher than heating clamber (3), and the horizontal location of the center of gravity of cooler (6) is higher than vaporization chamber (4).
2. the efficient percolating extractor of one according to claim 1, it is characterized in that: the steam outlet of vaporization chamber (4) is provided with pressure detector, described percolation filtration extraction pot (1) is also provided with solvent pair and adds mouth, and described solvent pair is added mouth and is used for the supplementing solvent when pressure detector detects insufficient pressure.
3. the efficient percolating extractor of one according to claim 1, it is characterized in that: the steam outlet of vaporization chamber (4) is provided with pressure detector, described cooler (6) is also provided with solvent pair and adds mouth, and described solvent pair is added mouth and is used for the supplementing solvent when pressure detector detects insufficient pressure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520454548.3U CN204734981U (en) | 2015-06-29 | 2015-06-29 | High -efficient diacolation extraction element |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520454548.3U CN204734981U (en) | 2015-06-29 | 2015-06-29 | High -efficient diacolation extraction element |
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| Publication Number | Publication Date |
|---|---|
| CN204734981U true CN204734981U (en) | 2015-11-04 |
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| CN201520454548.3U Active CN204734981U (en) | 2015-06-29 | 2015-06-29 | High -efficient diacolation extraction element |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111450570A (en) * | 2020-04-09 | 2020-07-28 | 尹亮 | Method for extracting herbal liquid |
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2015
- 2015-06-29 CN CN201520454548.3U patent/CN204734981U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111450570A (en) * | 2020-04-09 | 2020-07-28 | 尹亮 | Method for extracting herbal liquid |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |