CN207641024U - A kind of drug distillation enrichment facility - Google Patents
A kind of drug distillation enrichment facility Download PDFInfo
- Publication number
- CN207641024U CN207641024U CN201721418214.6U CN201721418214U CN207641024U CN 207641024 U CN207641024 U CN 207641024U CN 201721418214 U CN201721418214 U CN 201721418214U CN 207641024 U CN207641024 U CN 207641024U
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- CN
- China
- Prior art keywords
- destilling tower
- drug
- enrichment facility
- heating mantle
- heating
- 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, the condensation for drug distillation steam to be carried out to condensing recovery, it is characterised in that:The heating component includes kiln Steam Recovery device, the heating mantle being sheathed on outside destilling tower, the outer wall of the destilling tower is the heat conductive wall with heat transmission function, the heating mantle bottom is provided with air inlet pipe, the top of heating mantle is provided with escape pipe, and the outlet of the kiln Steam Recovery device is connect with air inlet pipe.The utility model provides a kind of drug distillation enrichment facility, can reduce energy consumption, be conducive to energy conservation and environmental protection.
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, energy consumption can be reduced, be conducive to energy conservation and environmental protection.
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, for drug to be distilled steam
Carry out the condensation of condensing recovery, it is characterised in that:The heating component includes kiln Steam Recovery device, is sheathed on destilling tower
The outer wall of external heating mantle, the destilling tower is the heat conductive wall with heat transmission function, and the heating mantle bottom is provided with air inlet
Pipe, the top of heating mantle are provided with escape pipe, and the outlet of the kiln Steam Recovery device is connect with air inlet pipe.
As an improvement, switch valve and flow control valve are provided in the air inlet pipe, using switch valve in heating mantle
The switch of heating steam is controlled, and using flow control valve, control enters the amount of heating steam.
It improves again, the heating mantle is provided with a thermometer gauge, and the bottom of the destilling tower is provided with a flask, flask
Outside is provided with an auxiliary electro-heat set, by the way that thermometer gauge is arranged, the temperature conditions in heating mantle is monitored, when in heating mantle
When set temperature is not achieved in temperature, auxiliary electro-heat covers work, improves the temperature in destilling tower.
It improves again, charge door is provided at the top of the destilling tower, vertical arranged for interval has multiple cross in the destilling tower
Plate, the outer end of each transverse slat are vertically provided with a baffle, adjacent two transverse slat interlaced arrangements, and steam is offered on each transverse slat
Hole, medicinal material enter from the charge door of destilling tower, and medicinal material is first piled up on the transverse slat on destilling tower top, the accumulation of top transverse slat medicinal material
Afterwards, from top, transverse slat is fallen on the transverse slat of lower section, and the utility model passes through the multiple cross of vertical interlaced arrangement in destilling tower
Medicinal material in destilling tower is separated by plate, avoids the accumulation of medicinal material in destilling tower.
It improves again, the condensation includes a supervisor being connected with destilling tower top, is connected to there are two branch pipe on supervisor,
The outer end of each branch pipe is connected with a condenser, and cooling collar is provided in condenser, a drug is connected with below condenser
Collector.The utility model corresponds to a condenser by the way that two branch pipes, each branch pipe are arranged above destilling tower, realizes to steaming
It evaporates the reduced vapor that tower is responsible for out to be shunted, improves the reduced vapor organic efficiency come out from destilling tower, ensure concentration
Steam carries out cooling recycling in time, rapidly.
Compared with prior art, the utility model has the advantage of:The hot gas that the utility model is generated using kiln as
Heat source heats destilling tower outer wall, by using the heat conductive wall with high thermal conductivity energy, realizes to the medicine in destilling tower
Material carries out distillation and concentration, and the direct emission for avoiding kiln hot gas damages environment, meanwhile, using kiln hot gas as medicine
The heat source of object distillation and concentration can reduce energy consumption, be conducive to energy conservation and environmental protection.
Description of the drawings
Fig. 1 is the structural schematic diagram of drug distillation and concentration device 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, drug in this implementation distills enrichment facility, include for holding medicine destilling tower 2, for pair
Heating component that 2 drug of destilling tower is heated, the condensation for drug distillation steam to be carried out to condensing recovery.
Wherein, heating component includes kiln Steam Recovery device 4, the heating mantle 1 being sheathed on outside destilling tower 2, the distillation
The outer wall of tower 2 is the heat conductive wall with heat transmission function, and 1 bottom of the heating mantle is provided with air inlet pipe 11, is arranged in air inlet pipe 11
There are switch valve 112 and flow control valve 111, the switch of the heating steam in heating mantle 1 controlled using switch valve 112,
Using flow control valve 111, control enters the amount of heating steam, and the top of heating mantle 1 is provided with escape pipe 12, and the kiln steams
The outlet of vapour recover 4 is connect with air inlet pipe 11.
Condensation includes a supervisor 5 being connected with 2 top of destilling tower, and being responsible for connection on 5, there are two branch pipes 51, Mei Gezhi
The outer end of pipe 51 is connected with a condenser 6, and cooling collar 7 is provided in condenser 6, and the lower section of condenser 6 is connected with a drug
Collector 8.The utility model corresponds to a condenser 7 by the way that two branch pipes 51, each branch pipe 51 are arranged above destilling tower 2,
It realizes and the reduced vapor of the supervisor of destilling tower 2 51 out is shunted, improve the reduced vapor recycling come out from destilling tower 2
Efficiency ensures that reduced vapor carries out cooling recycling in time, rapidly.
In addition, heating mantle 1 is provided with a thermometer gauge, the bottom of the destilling tower 2 is provided with a flask 201, flask
It is provided with auxiliary electro-heat set 3 outside 201, by the way that thermometer gauge is arranged, monitors the temperature conditions in heating mantle 1, works as heating
When set temperature is not achieved in temperature in set 1,3 work of auxiliary electro-heat set improves the temperature in destilling tower 2.
In addition, the top of destilling tower 2 is provided with charge door 22, vertical arranged for interval has multiple transverse slats in the destilling tower 2
21, the outer end of each transverse slat 21 is vertically provided with a baffle 211, adjacent two 21 interlaced arrangements of transverse slat, on each transverse slat 21
Steam hole is offered, medicinal material enters from the charge door 22 of destilling tower 2, and medicinal material is first piled up on the transverse slat 21 on 2 top of destilling tower,
After the transverse slat medicinal material accumulation of top, from top, transverse slat is fallen on the transverse slat of lower section, and the utility model in destilling tower 2 by erecting
To the multiple transverse slats 21 of interlaced arrangement, the medicinal material in destilling tower 2 is separated, the accumulation of medicinal material in destilling tower 2 is avoided.
The hot gas that the utility model is generated using kiln heats 2 outer wall of destilling tower as heat source, by using tool
There is the heat conductive wall of high thermal conductivity energy, realizes and distillation and concentration is carried out to the medicinal material in destilling tower 2, avoid the direct of kiln hot gas
Discharge damages environment, meanwhile, the heat source using kiln hot gas as drug distillation and concentration can reduce energy consumption,
Be conducive to energy conservation and environmental protection.
Claims (5)
1. a kind of drug distills enrichment facility, include for holding medicine destilling tower (2), for destilling tower (2) drug into
The heating component of row heating, the condensation for drug distillation steam to be carried out to condensing recovery, it is characterised in that:The heating
Component includes kiln Steam Recovery device (4), is sheathed on the heating mantle (1) of destilling tower (2) outside, the outer wall of the destilling tower (2)
For the heat conductive wall with heat transmission function, heating mantle (1) bottom is provided with air inlet pipe (11), the top setting of heating mantle (1)
There are escape pipe (12), the outlet of the kiln Steam Recovery device (4) to be connect with air inlet pipe (11).
2. drug according to claim 1 distills enrichment facility, it is characterised in that:It is provided with out on the air inlet pipe (11)
Close valve (112) and flow control valve (111).
3. drug according to claim 2 distills enrichment facility, it is characterised in that:The heating mantle (1) is provided with a temperature
Quantifier is spent, the bottom of the destilling tower (2) is provided with flask (201), an auxiliary electro-heat set is provided with outside flask (201)
(3)。
4. drug according to claim 3 distills enrichment facility, it is characterised in that:The top of the destilling tower (2) is arranged
There is a charge door (22), vertical arranged for interval has multiple transverse slats, the outer end of each transverse slat (21) vertically arranged in the destilling tower (2)
There is a baffle (211), adjacent two transverse slat (21) interlaced arrangements offer steam hole on each transverse slat (21).
5. drug according to claim 4 distills enrichment facility, it is characterised in that:The condensation includes one and distillation
Connected supervisor (5) at the top of tower (2), being responsible for connection on (5), there are two branch pipes (51), and the outer end of each branch pipe (51) is connected with one
Condenser (6), condenser (6) is interior to be provided with cooling collar (7), and a drug collector (8) is connected with below condenser (6).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721418214.6U CN207641024U (en) | 2017-10-30 | 2017-10-30 | A kind of drug distillation enrichment facility |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721418214.6U CN207641024U (en) | 2017-10-30 | 2017-10-30 | A kind of drug distillation enrichment facility |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207641024U true CN207641024U (en) | 2018-07-24 |
Family
ID=62883986
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201721418214.6U Expired - Fee Related CN207641024U (en) | 2017-10-30 | 2017-10-30 | A kind of drug distillation enrichment facility |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207641024U (en) |
-
2017
- 2017-10-30 CN CN201721418214.6U patent/CN207641024U/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 | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180724 Termination date: 20191030 |