CN205360630U - Sliced medicinal herbs decocte liquid enrichment facility - Google Patents
Sliced medicinal herbs decocte liquid enrichment facility Download PDFInfo
- Publication number
- CN205360630U CN205360630U CN201620089403.2U CN201620089403U CN205360630U CN 205360630 U CN205360630 U CN 205360630U CN 201620089403 U CN201620089403 U CN 201620089403U CN 205360630 U CN205360630 U CN 205360630U
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- concentration tank
- extracting solution
- mounting head
- enrichment facility
- conveying pipe
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Abstract
The utility model discloses a sliced medicinal herbs decocte liquid enrichment facility, assist hot heating furnace, booster pump and negative -pressure air fan including concentrated jar, air compressor machine, electricity, install on concentrated tank support for concentrated jar, top one side of concentrated jar is equipped with the extract conveyer pipe, and the one end of extract conveyer pipe connects extract conveying equipment, the other end extend to concentrated jar inside, and the extract conveyer pipe extends to concentrated jar of inside structural a plurality of atomizers that are equipped with, the atomizer communicates with each other with the extract conveyer pipe is inside, the utility model discloses rational in infrastructure, whole heat transfer is fast, and concentration efficiency is very high, and the filtration of entry end and exit end makes and has wholly avoided blocking phenomenon simultaneously, and whole filter core can all conveniently be looked over and change moreover, therefore follow -up maintenance is more convenient.
Description
Technical field
This utility model relates to Chinese drug preparation equipment, specifically a kind of decoction pieces decoction liquor enrichment facility.
Background technology
Decoction pieces refers to Chinese medicine as required, the Chinese medicine for formula formed through process of preparing Chinese medicine process, or can be directly used for the Chinese medicine of tcm clinical practice.The prepared slices of Chinese crude drugs are the elite places of Chinese medicine, and medical material is through different concocting methods, and its property of medicine and effect can change, and are feature and the advantage of middle medical drugs.
Decoction pieces needs to decoct more in actually used process, owing to decoction process is loaded down with trivial details, the slice decoction that normal conditions patient decocts voluntarily is difficult to reach actual demand, the property of medicine is subject to water excess dilution in the process simultaneously, therefore patient needs to drink substantial amounts of decoction mostly, so not only make patient very uncomfortable, and effect also very bad；Therefore existing medicine is looked forward under carrying out various research, it is pregnant with decoction pieces decoction liquor enrichment facility, the concentrated solution produced both had had good therapeutic effect, simultaneously dosage also lacking very, but current concentrator ubiquity problem, wherein essentially consists in concentrator and the problem of medicinal residues blocking discharging tube easily occurs, cause overall yield not high, later maintenance process is numerous and diverse, and the power consumption of entirety is excessive.
Utility model content
The purpose of this utility model is in that to provide a kind of decoction pieces decoction liquor enrichment facility, with the problem solving to propose in above-mentioned background technology.
For achieving the above object, this utility model provides following technical scheme:
A kind of decoction pieces decoction liquor enrichment facility, including concentration tank, the mechanical, electrical auxiliary hot heating furnace of pneumatics, booster pump and negative-pressure air fan, described concentration tank is installed on concentration tank support, the upper side of concentration tank is provided with extracting solution conveying pipe, and one end of extracting solution conveying pipe connects extracting solution conveying equipment, the other end extends to inside concentration tank, and extracting solution conveying pipe extends to the structure within concentration tank and is provided with multiple atomizer, and atomizer is carried with extracting solution and communicated inside pipe；Extracting solution conveying pipe is provided with booster pump, and the porch of booster pump is provided with filter mounting head, the upper end of filter mounting head is provided with mounting head upper cover, and mounting head upper cover is by being connected with the handwheel screw of screw rod and filter mounting head are fixing, therefore the filter element in filter mounting head can conveniently select to change；The outfan of described air compressor machine connects the auxiliary hot heating furnace of electricity, the auxiliary hot heating furnace of electricity connects airway, the end of airway connects jet disk, and jet disk is located at the underface of atomizer, therefore in the process of reality concentration, by air compressor machine conveying compression air, compression air is through the quick heating of the auxiliary hot heating furnace of electricity simultaneously, and upwards spray at a high speed through jet disk, now the extracting solution after booster pump supercharging is through atomizer atomization ejection, extracting solution after atomization and high pressure draught realize rapidly heat exchange, solvent in extracting solution then can realize evaporation at a high speed；The upper end of concentration tank is provided with exhaustor, and negative-pressure air fan is located on exhaustor, and the solvent of evaporation is then discharged under condition of negative pressure, and condition of negative pressure also contributes to the evaporation of solvent simultaneously.
As further program of the utility model: the bottom of described concentration tank is provided with concentrated solution and extracts mouth, and concentrated solution extracts that mouth place is threaded concentrated solution filter, utilizing concentrated solution filter to realize further filtering, occurring thus avoiding stopping state.
As this utility model further scheme: the bottom of described concentration tank adopts cone structure, it is simple to the concentration of extracting solution obtains.
As this utility model further scheme: described concentration tank is that tank skin adopts vacuum interlayer structure, and integral heat insulation is strong, it is simple to centralized head load.
Compared with prior art, the beneficial effects of the utility model are: this utility model is rational in infrastructure, overall heat exchange speed is fast, thickening efficiency is significantly high, the filtration of arrival end and the port of export makes entirety avoid clogging simultaneously, and whole filter element can conveniently be checked and change, therefore follow-up maintenance is convenient.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of decoction pieces decoction liquor enrichment facility of this utility model.
In figure: 1-concentration tank support, 2-concentration tank, 3-air compressor machine, the 4-auxiliary hot heating furnace of electricity, 5-airway, 6-jet disk, 7-extracting solution conveying pipe, 8-filter mounting head, 9-mounting head upper cover, 10-handwheel screw, 11-booster pump, 12-atomizer, 13-exhaustor, 14-negative-pressure air fan, 15-concentrated solution extract mouth, 16-concentrated solution filter.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is clearly and completely described, it is clear that described embodiment is only a part of embodiment of this utility model, rather than whole embodiments.Based on the embodiment in this utility model, the every other embodiment that those of ordinary skill in the art obtain under not making creative work premise, broadly fall into the scope of this utility model protection.
Refer to Fig. 1, in this utility model embodiment, a kind of decoction pieces decoction liquor enrichment facility, including concentration tank 2, air compressor machine 3, the auxiliary hot heating furnace 4 of electricity, booster pump 11 and negative-pressure air fan 14, described concentration tank 2 is installed on concentration tank support 1, the upper side of concentration tank 2 is provided with extracting solution conveying pipe 7, and one end of extracting solution conveying pipe 7 connects extracting solution conveying equipment, it is internal that the other end extends to concentration tank 2, and extracting solution conveying pipe 7 extends to the structure within concentration tank 2 and is provided with multiple atomizer 12, atomizer 12 carries pipe 7 inside to communicate with extracting solution；Extracting solution conveying pipe 7 is provided with booster pump 11, and the porch of booster pump 11 is provided with filter mounting head 8, the upper end of filter mounting head 8 is provided with mounting head upper cover 9, and mounting head upper cover 9 is by being connected with the handwheel screw 10 of screw rod is fixing with filter mounting head 8, therefore the filter element in filter mounting head 8 can conveniently select to change；The outfan of described air compressor machine 3 connects the auxiliary hot heating furnace 4 of electricity, the auxiliary hot heating furnace 4 of electricity connects airway 5, the end of airway 5 connects jet disk 6, and jet disk 6 is located at the underface of atomizer 12, therefore in the process of reality concentration, by air compressor machine 3 conveying compression air, compression air is through the quick heating of the auxiliary hot heating furnace 4 of electricity simultaneously, and upwards spray at a high speed through jet disk 6, now the extracting solution after booster pump 11 supercharging is through atomizer 12 atomization ejection, extracting solution after atomization and high pressure draught realize rapidly heat exchange, solvent in extracting solution then can realize evaporation at a high speed；The upper end of concentration tank 2 is provided with exhaustor 13, and negative-pressure air fan 14 is located on exhaustor 13, and the solvent of evaporation is then discharged under condition of negative pressure, and condition of negative pressure also contributes to the evaporation of solvent simultaneously.
The bottom of described concentration tank 2 is provided with concentrated solution and extracts mouth 15, and concentrated solution extracts that mouth 15 place is threaded concentrated solution filter 16, utilizing concentrated solution filter 16 to realize further filtration, occurring thus avoiding stopping state.
The bottom of described concentration tank 2 adopts cone structure, it is simple to the concentration of extracting solution obtains.
Described concentration tank 2 adopts vacuum interlayer structure for tank skin, and integral heat insulation is strong, it is simple to centralized head load.
Operation principle of the present utility model is: therefore in the process of reality concentration, by air compressor machine 3 conveying compression air, compression air is through the quick heating of the auxiliary hot heating furnace 4 of electricity simultaneously, and upwards spray at a high speed through jet disk 6, now the extracting solution after booster pump 11 supercharging is through atomizer 12 atomization ejection, extracting solution after atomization and high pressure draught realize rapidly heat exchange, solvent in extracting solution then can realize evaporation at a high speed, the solvent sent out then is discharged under condition of negative pressure, condition of negative pressure also contributes to the evaporation of solvent simultaneously, filtration in filter mounting head 8 can effectively prevent stopping state in the process, filter element in middle filtrator mounting head 8 can be convenient for changing simultaneously, concentrated solution filter 16 realizes further filtration, occur thus avoiding bottom stopping state.
It is obvious to a person skilled in the art that this utility model is not limited to the details of above-mentioned one exemplary embodiment, and when without departing substantially from spirit of the present utility model or basic feature, it is possible to realize this utility model in other specific forms.Therefore, no matter from which point, embodiment all should be regarded as exemplary, and be nonrestrictive, scope of the present utility model is limited by claims rather than described above, it is intended that all changes in the implication of the equivalency dropping on claim and scope included in this utility model.Any accompanying drawing labelling in claim should be considered as the claim that restriction is involved.
In addition, it is to be understood that, although this specification is been described by according to embodiment, but not each embodiment only comprises an independent technical scheme, this narrating mode of description is only for clarity sake, description should be made as a whole by those skilled in the art, and the technical scheme in each embodiment through appropriately combined, can also form other embodiments that it will be appreciated by those skilled in the art that.
Claims (4)
1. a decoction pieces decoction liquor enrichment facility, including concentration tank (2), air compressor machine (3), the auxiliary hot heating furnace (4) of electricity, booster pump (11) and negative-pressure air fan (14), it is characterized in that, described concentration tank (2) is installed on concentration tank support (1), the upper side of concentration tank (2) is provided with extracting solution conveying pipe (7), and one end of extracting solution conveying pipe (7) connects extracting solution conveying equipment, it is internal that the other end extends to concentration tank (2), and the structure that extracting solution conveying pipe (7) extends to concentration tank (2) internal is provided with multiple atomizer (12), atomizer (12) is internal with extracting solution conveying pipe (7) to communicate；Extracting solution conveying pipe (7) is provided with booster pump (11), and the porch of booster pump (11) is provided with filter mounting head (8), the upper end of filter mounting head (8) is provided with mounting head upper cover (9), and mounting head upper cover (9) is by being connected with the handwheel screw (10) of screw rod and filter mounting head (8) are fixing, the outfan of described air compressor machine (3) connects the auxiliary hot heating furnace (4) of electricity, the auxiliary hot heating furnace (4) of electricity connects airway (5), the end of airway (5) connects jet disk (6), and jet disk (6) is located at the underface of atomizer (12)；The upper end of concentration tank (2) is provided with exhaustor (13), and negative-pressure air fan (14) is located on exhaustor (13).
2. decoction pieces decoction liquor enrichment facility according to claim 1, it is characterised in that the bottom of described concentration tank (2) is provided with concentrated solution and extracts mouth (15), and concentrated solution extracts, and mouth (15) place is threaded concentrated solution filter (16).
3. decoction pieces decoction liquor enrichment facility according to claim 1, it is characterised in that the bottom of described concentration tank (2) adopts cone structure.
4. decoction pieces decoction liquor enrichment facility according to claim 1, it is characterised in that described concentration tank (2) adopts vacuum interlayer structure for tank skin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620089403.2U CN205360630U (en) | 2016-01-28 | 2016-01-28 | Sliced medicinal herbs decocte liquid enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620089403.2U CN205360630U (en) | 2016-01-28 | 2016-01-28 | Sliced medicinal herbs decocte liquid enrichment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205360630U true CN205360630U (en) | 2016-07-06 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620089403.2U Expired - Fee Related CN205360630U (en) | 2016-01-28 | 2016-01-28 | Sliced medicinal herbs decocte liquid enrichment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205360630U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108404435A (en) * | 2018-03-08 | 2018-08-17 | 江苏师范大学 | A kind of cold concentration tower |
| CN108969360A (en) * | 2018-06-13 | 2018-12-11 | 温州医科大学 | A kind of Traditional Chinese medicine decoction boiler and Traditional Chinese medicine decocting method based on high pressure and multilayer |
-
2016
- 2016-01-28 CN CN201620089403.2U patent/CN205360630U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108404435A (en) * | 2018-03-08 | 2018-08-17 | 江苏师范大学 | A kind of cold concentration tower |
| CN108969360A (en) * | 2018-06-13 | 2018-12-11 | 温州医科大学 | A kind of Traditional Chinese medicine decoction boiler and Traditional Chinese medicine decocting method based on high pressure and multilayer |
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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: 20160706 Termination date: 20190128 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |