CN207614373U - Drug distills enrichment facility - Google Patents
Drug distills enrichment facility Download PDFInfo
- Publication number
- CN207614373U CN207614373U CN201721417051.XU CN201721417051U CN207614373U CN 207614373 U CN207614373 U CN 207614373U CN 201721417051 U CN201721417051 U CN 201721417051U CN 207614373 U CN207614373 U CN 207614373U
- Authority
- CN
- China
- Prior art keywords
- destilling tower
- distillation
- drug
- distills
- enrichment facility
- 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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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a kind of drugs to distill enrichment facility, includes the destilling tower for holding medicine, the heating component for being heated to destilling tower drug, it is characterised in that：The heating component includes electric jacket, the bottom of the destilling tower is provided with flask, flask is set in electric jacket, distillation supervisor is connected at the top of the destilling tower, the distillation supervisor is above radial to be connected with multiple distillation branch pipes, a condensation for drug distillation steam to be carried out to condensing recovery is connected on each distillation branch pipe, each condensation includes and the condenser of corresponding distillation branch pipe connection, the cooling collar being set in condenser, the drug collector being set to below condenser.The utility model provides a kind of drug distillation enrichment facility, improves the reduced vapor organic efficiency come out from destilling tower, ensures that reduced vapor carries out cooling recycling in time, rapidly.
Description
Technical field
The utility model is related to medical field of mechanical technique more particularly to a kind of drug to distill enrichment facility.
Background technology
Since medicinal material this body tissue has a capillarity between absorbency and powder, the active ingredient of medicinal material is not easy point
From, it is generally the case that the amount of active ingredient is considerable in these medicinal materials, and is worth with recycling very well, existing skill
Art recycles dregs of a decoction solvent generally directed to medicinal material using direct expression, displacement method, but recovering effect is bad, and cost input
Height, the solvent rate of recovery is low, or even is mixed with various impurity in the solvent after recycling, is brought much not to the processing of follow-up solvent
Just.
Distillation and concentration refers to that solution heating is made solvent evaporation in distiller, is concentrated simultaneously by condensing recovery solvent molten
The method of liquid, for this purpose, people are handled medicinal material using the method for distillation and concentration.For example, existing Patent No.
The Chinese utility model of ZL201120398778.4 discloses《A kind of small-sized low-temperature-boiling decocting, extractor》Including band heating dress
The kettle of boiling medicine set, the kettle upper end of boiling medicine are connected to negative pressure pump by negative pressure line, check-valves and valve are arranged in the negative pressure line
Door.The utility model can realize that the closed liquid boiled medicine in kettle boils under low-temperature vacuum environment, keep unstable Chinese medicine effective
Ingredient is non-volatile, does not aoxidize and is not pyrolyzed, free from environmental pollution, and effective component of chinese medicine dissolution is fast, and recovery rate is high, and effect of boiling medicine is good,
It is simple to operate, save the time, it is energy saving, it is at low cost the advantages that, be conducive to promote and apply.
However, the existing method and apparatus extracted to effective ingredient using distillation and concentration method, the following
Problem：1, existing general using electricity heat or generate heat, energy using coal burning using distillation and concentration method
Consumption consumption is big, is unfavorable for energy saving；2, the reduced vapor organic efficiency come out from destilling tower is relatively low, will cannot rapidly concentrate in time
Steam cooling recycling；3, medicinal material is accumulated in destilling tower, and cannot obtain good distillation and concentration to the medicinal material inside destilling tower imitates
Fruit.
Utility model content
The technical problems to be solved in the utility model is the present situation for the prior art, provides a kind of drug distillation and concentration dress
It sets, improves the reduced vapor organic efficiency come out from destilling tower, ensure that reduced vapor carries out cooling recycling in time, rapidly.
Technical solution is used by the utility model solves above-mentioned technical problem：A kind of drug distillation enrichment facility, packet
Include the destilling tower for holding medicine, the heating component for being heated to destilling tower drug, it is characterised in that：The heating
Component includes electric jacket, and the bottom of the destilling tower is provided with flask, and flask is set in electric jacket, the top of the destilling tower
It is connected with distillation supervisor, the distillation supervisor is above radial to be connected with multiple distillation branch pipes, and each distill is connected on branch pipe
One condensation for drug distillation steam to be carried out to condensing recovery, each condensation includes connecting with corresponding distillation branch pipe
Logical condenser, the cooling collar being set in condenser, the drug collector being set to below condenser.
As an improvement, being provided with feeding port at the top of the destilling tower, it is provided with a charging ladder by the destilling tower, leads to
Setting charging ladder is crossed, when adding medicinal material, worker can climb up charging ladder, and medicinal material is carried to the feeding port of destilling tower
Destilling tower feeding is convenient at place.
It improves again, the lower part of the destilling tower is provided with discharge port, and discharge gate is provided on discharge port, is distilled in medicinal material
After concentration, discharge gate is opened, the medicinal material in destilling tower can come out in discharging out of destilling tower.
It improves again, a heating mantle moved up and down is arranged on the outer wall of the destilling tower, by the way that heating mantle is arranged, be convenient for
Partial section on destilling tower is heated, partial distillation concentrated effect is improved.
It improves again, bottom is provided with a backgauge orifice plate in the destilling tower, there is more vertical arranged for interval in the destilling tower
A transverse slat, the outer end of each transverse slat are vertically provided with a baffle, adjacent two transverse slat interlaced arrangements, are offered on each transverse slat
Steam hole.Medicinal material enters from the feeding port of destilling tower, and medicinal material is first piled up on the transverse slat on destilling tower top, top transverse slat medicinal material
After accumulation, from top transverse slat fall to lower section transverse slat on, the utility model by destilling tower vertical interlaced arrangement it is more
Medicinal material in destilling tower is separated by a transverse slat, avoids the accumulation of medicinal material in destilling tower.
It improves again, the baffle is located at the downside of transverse slat, and the height of baffle is no more than the height of corresponding transverse slat, to anti-
Blocking of the baffle to medicinal material on corresponding transverse slat is stopped.
Compared with prior art, the utility model has the advantage of：The utility model is steamed in the top of destilling tower setting one
Evaporate supervisor, by the upper radial multiple distillation branch pipes of connection of distillation supervisor, in this way, by out of destilling tower distillation and concentration come out
Within steam diversion to each distillation branch pipe, realization shunts the reduced vapor that destilling tower is responsible for out, then passes through correspondence
Each condenser carry out condensing recovery, to improve from destilling tower come out reduced vapor organic efficiency, ensure concentration steam
Vapour carries out cooling recycling in time, rapidly.
Description of the drawings
Fig. 1 is the structural schematic diagram of drug distillation and concentration device in the utility model embodiment；
Fig. 2 is the vertical view of each distillation branch pipe on destilling tower in the utility model embodiment.
Specific implementation mode
The utility model is described in further detail below in conjunction with attached drawing embodiment.
As shown in Figure 1, 2, the drug in this implementation distills enrichment facility, including destilling tower 1, heating component, multiple condensations
Component.
Wherein, destilling tower 1 is used for holding medicine, and heating component is for heating 1 drug of destilling tower, heating component packet
Electric jacket 2 is included, the bottom of the destilling tower 1 is provided with flask 11, and flask 11 is set in electric jacket 2, the top of the destilling tower 1
Portion is connected with distillation supervisor 15, radial on distillation supervisor 15 to be connected with multiple distillation branch pipes 3, each distillation branch pipe 3
On be connected with a condensation for drug distillation steam to be carried out to condensing recovery, each condensation includes and corresponding steaming
The condenser 4 for evaporating the connection of branch pipe 3, the cooling collar 5 being set in condenser 4, the drug collector for being set to 4 lower section of condenser
6。
In addition, the top of destilling tower 1 is provided with feeding port 14, a charging ladder is provided with by the destilling tower 1, by setting
Charging ladder is set, when adding medicinal material, worker can climb up charging ladder, medicinal material is carried at the feeding port of destilling tower 1, just
In 1 feeding of destilling tower；Meanwhile the lower part of destilling tower 1 is provided with discharge port 17, and discharge gate 171 is provided on discharge port 17,
After medicinal material distillation and concentration, discharge gate 171 is opened, the medicinal material in destilling tower 1 can come out in discharging out of destilling tower 1.
In addition, being arranged with a heating mantle 13 moved up and down on the outer wall of destilling tower 1, by the way that heating mantle 13 is arranged, it is convenient for
Partial section on destilling tower 1 is heated, partial distillation concentrated effect is improved.
In addition, bottom is provided with a backgauge orifice plate 16 in destilling tower 1, there is multiple vertical arranged for interval in the destilling tower 1
The outer end of transverse slat 12, each transverse slat 12 is vertically provided with a baffle 121, adjacent two 12 interlaced arrangements of transverse slat, each transverse slat
Steam hole is offered on 12.Medicinal material enters from the feeding port 14 of destilling tower 1, and medicinal material is first piled up in the transverse slat 12 on 1 top of destilling tower
On, after the accumulation of top transverse slat medicinal material, from top, transverse slat is fallen on the transverse slat of lower section, and the utility model passes through in destilling tower
The vertical multiple transverse slats 12 of interlaced arrangement, the medicinal material in destilling tower 1 is separated, the heap of medicinal material in destilling tower 1 is avoided in 1
Product；Further, baffle 121 is located at the downside of transverse slat 12, and the height of baffle 121 is no more than the height of corresponding transverse slat 12, from
And prevent blocking of the baffle 121 to medicinal material on corresponding transverse slat 12.
The utility model passes through the radial company on distillation supervisor 15 in one distillation supervisor 15 of the top of destilling tower 1 setting
Lead to multiple distillation branch pipes 3, in this way, by out of destilling tower 1 distillation and concentration out steam diversion to each distillation branch pipe 3 within,
It realizes and the reduced vapor of destilling tower supervisor 15 out is shunted, then condensing recovery is carried out by corresponding each condenser 4,
To improve the reduced vapor organic efficiency come out from destilling tower 1, ensures that reduced vapor is timely, rapidly cooled back
It receives.
Claims (6)
1. a kind of drug distills enrichment facility, include for holding medicine destilling tower (1), for destilling tower (1) drug into
The heating component of row heating, it is characterised in that：The heating component includes electric jacket (2), the bottom setting of the destilling tower (1)
There are flask (11), flask (11) to be set in electric jacket (2), distillation supervisor (15) be connected at the top of the destilling tower (1),
It is radial on distillation supervisor (15) to be connected with multiple distillation branch pipes (3), it each distills and is connected with one on branch pipe (3) be used for will
Drug distills the condensation that steam carries out condensing recovery, and each condensation includes being connected to corresponding distillation branch pipe (3)
Condenser (4), the cooling collar (5) being set in condenser (4), the drug collector (6) being set to below condenser (4).
2. drug according to claim 1 distills enrichment facility, it is characterised in that：The top of the destilling tower (1) is arranged
There is feeding port (14), a charging ladder is provided with by the destilling tower (1).
3. drug according to claim 2 distills enrichment facility, it is characterised in that：It is covered on the outer wall of the destilling tower (1)
The heating mantle (13) moved up and down equipped with one.
4. drug according to claim 3 distills enrichment facility, it is characterised in that：The interior bottom setting of destilling tower (1)
There is a backgauge orifice plate (16), vertical arranged for interval has multiple transverse slats (12), the outer end of each transverse slat (12) in the destilling tower (1)
It is vertically provided with a baffle (121), adjacent two transverse slat (12) interlaced arrangements offer steam hole on each transverse slat (12).
5. drug according to claim 4 distills enrichment facility, it is characterised in that：The baffle (121) is located at transverse slat
(12) downside, the height of baffle (121) are no more than the height of corresponding transverse slat (12).
6. drug according to claim 4 distills enrichment facility, it is characterised in that：The lower part of the destilling tower (1) is arranged
There is discharge port (17), discharge gate (171) is provided on discharge port (17).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721417051.XU CN207614373U (en) | 2017-10-30 | 2017-10-30 | Drug distills enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721417051.XU CN207614373U (en) | 2017-10-30 | 2017-10-30 | Drug distills enrichment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207614373U true CN207614373U (en) | 2018-07-17 |
Family
ID=62827132
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721417051.XU Expired - Fee Related CN207614373U (en) | 2017-10-30 | 2017-10-30 | Drug distills enrichment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207614373U (en) |
-
2017
- 2017-10-30 CN CN201721417051.XU patent/CN207614373U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180717 Termination date: 20191030 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |