CN206240114U - One kind extracts concentration systems - Google Patents
One kind extracts concentration systems Download PDFInfo
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- CN206240114U CN206240114U CN201621362229.0U CN201621362229U CN206240114U CN 206240114 U CN206240114 U CN 206240114U CN 201621362229 U CN201621362229 U CN 201621362229U CN 206240114 U CN206240114 U CN 206240114U
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- concentration
- condenser
- collection system
- concentration systems
- tank
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Abstract
The utility model provides a kind of extraction concentration systems,Including concentration systems,Condenser system,Collection system,Concentration systems include cooker,Filter,Concentration tank,Condenser system includes the condenser I being sequentially connected,Gas-liquid separator I,Condenser II,Gas-liquid separator II,Condenser I is located at the top of concentration tank and is attached thereto,Gas-liquid separator II is connected with cooker,Collection system accepts the concentrate of concentration systems discharge,Collection system includes fine filtrator,Blending tank,Homogenizer,Coarse filter,Fine filtrator one end of collection system is connected with the concentration tank body exit of concentration systems,Concentrate sequentially passes through fine filtrator,Blending tank,Homogenizer and coarse filter are processed,The other density of setting meter on the concentration tank body of concentration systems,Concentrating degree in real-time monitoring concentration tank,Other external collection system,Stabilization processes are carried out to final extract solution state,Finally give in stable condition extraction concentrat.
Description
Technical field
The utility model is related to a kind of extraction concentration systems.
Background technology
Often to be concentrated using to extraction in the industries such as medicines and health protection, pigment, food and drink, animals and plants, chemical industry at present
Unit, extracts concentration unit main in normal pressure, decocting, immersion, hot backflow, circulation infiltration, fragrant oil extract and organic solvent time
Used in the operation of the kinds of processes such as receipts.There is problems with the extraction concentration unit for using at this stage, running：1st, raw material steams
During boiling down contracting, due to there is substantial amounts of thin impurity in extract, simple coarse filtration can only filter out raw material residue, to tiny
Impurity can not be filtered out, and extract has tiny residue and debris after final concentration, makes extract state labile, or even go out
Existing lamination；2nd, without the device for determining density at any time, it has not been convenient to be visually known concentration progress, terminate in final concentration,
The enrichment stage of extract solution cannot immediately be judged；3rd, the gas-liquid evaporated is not reclaimed, causes certain waste；4th, not to most
Whole extract solution state carries out stabilization processes, has sediment to occur in solution.
Utility model content
For above technological deficiency, the utility model provides a kind of extraction concentration systems, and the close of density is determined by installing additional
Concentrating degree in degree meter real-time monitoring concentration tank, external collection system, stabilization is carried out to final extract solution state in addition
Change is processed.
The technical solution adopted in the utility model is：One kind extracts concentration systems, including concentration systems, condenser system, receipts
Collecting system, concentration systems include cooker, filter, concentration tank, and condenser system includes the condenser I, the gas-liquid point that are sequentially connected
From device I, condenser II, gas-liquid separator II, condenser I be located at concentration tank top and be attached thereto, gas-liquid separator II with
Cooker is connected, and collection system accepts the concentrate of concentration systems discharge, and collection system includes fine filtrator, blending tank, homogeneous
Machine, coarse filter, fine filtrator one end of collection system are connected with the concentration tank body exit of concentration systems, and concentrate is passed through successively
Cross the treatment of fine filtrator, blending tank, homogenizer and coarse filter, the density of setting meter on the concentration tank body of concentration systems.
Preferably, the fine filtrator mesh number of collection system is 300-1000 mesh.
The beneficial effects of the utility model are：1st, the density of setting meter on concentration tank body, can intuitively observe concentration
Progress, judges the enrichment stage of extract solution；
The 2nd, condenser system is set, and the active ingredient being included in evaporation steam is reclaimed in condensed in two stages loop to greatest extent.
3rd, the extract flowed out by the concentration tank exit of concentration tank, is processed by collection system, obtains final shape
State stabilization, extraction concentrat in good taste.
Brief description of the drawings
Fig. 1 is idiographic flow schematic diagram of the present utility model.
In figure：1- cookers；2- filters；3- concentration tanks；4- condensers I；5- gas-liquid separators I；6- condensers II；7-
Gas-liquid separator II；8- fine filtrators；9- blending tanks；10- homogenizers；11- coarse filters.
Specific embodiment
Specific embodiment of the present utility model is further described below in conjunction with the accompanying drawings, as shown in figure 1, this practicality
New offer is a kind of to extract concentration systems, including concentration systems, condenser system, collection system, concentration systems include cooker 1,
Filter 2, concentration tank 3, condenser system include the condenser I4, gas-liquid separator I5, condenser II6, the gas-liquid point that are sequentially connected
From device II7, condenser I4 is located at the top of concentration tank 3 and is attached thereto, and gas-liquid separator II6 is connected with cooker 1, collects system
System accepts the concentrate of concentration systems discharge, and collection system includes fine filtrator 8, blending tank 9, homogenizer 10, coarse filter 11,
One end of fine filtrator 8 of collection system is connected with the body exit of concentration tank 3 of concentration systems, and concentrate sequentially passes through fine filtrator
8th, blending tank 9, homogenizer 10 and coarse filter 11 are processed, in addition the density of setting meter (in figure on the body of concentration tank 3 of concentration systems
It is not shown).
Further, the mesh number of fine filtrator 8 of collection system is 300-1000 mesh.
Operation principle of the present utility model is：Extract material and water to be entered by the material of cooker 1 mouthful, added by cooker 1
Hot boiling is extracted, and by filter 2, extract in cooker 1 is carried out into coarse filtration, enters back into concentration tank 3, and now vavuum pump will
Concentration tank 3 is vacuumized, and concentration tank 3 ceaselessly heats concentration, and the vapor of evaporation side is reached by condenser I4 on concentration tank 3
Gas-liquid separator I5, the condensed water isolated returns to concentration tank 3 by return duct, and the gas isolated again passes by condenser
II6 and gas-liquid separator II7, the liquid of condensation returns to evaporator 1 from gas-liquid separator II7, and the gas being again separate out is drained.
By condensing recovery twice, the loss of the active ingredient in concentration tank 3 in boil-off gas is prevented to greatest extent, improve and extract
Efficiency.
Extract exits into fine filtrator 8 by the exit of concentration tank 3, by filtering more than 300-1000 mesh, will be thin
Enter blending tank 9 after small particulate matter filtering, can will now need the auxiliary material of addition to carry out dissolving addition and be sufficiently stirred for, then will
Solution stable state of the concentrate that supplementary material is added after homogenizer 10 further concentrates extraction, if while extracted
Material is some Chinese medicines etc, and extract can produce the end-state of the influence extract such as a large amount of foams in homogenizing process, this
When can further be defoamed by coarse filter 11 again, finally give in stable condition, in good taste extraction concentrat.
The foregoing is only preferred embodiment of the present utility model, it is noted that for the ordinary skill people of this area
For member, on the premise of the utility model creation design is not departed from, deformation can also be made and improved, should all belong to this practicality
New protection domain.
Claims (2)
1. a kind of to extract concentration systems, including concentration systems, condenser system, collection system, described concentration systems include boiling
Tank, filter, concentration tank, it is characterised in that：Described condenser system include be sequentially connected condenser I, gas-liquid separator I,
Condenser II, gas-liquid separator II, described condenser I are located at the top of concentration tank and are attached thereto, described gas-liquid separation
Device II is connected with cooker, and described collection system accepts the concentrate of concentration systems discharge, and described collection system includes thin
Filter, blending tank, homogenizer, coarse filter, fine filtrator one end of the collection system and the concentration tank body of concentration systems
Exit is connected, and concentrate sequentially passes through the treatment of fine filtrator, blending tank, homogenizer and coarse filter, in the concentration systems
Concentration tank body on density of setting meter.
2. extraction concentration systems according to claim 1, it is characterised in that：The fine filtrator mesh number of the collection system is
300-1000 mesh.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621362229.0U CN206240114U (en) | 2016-12-02 | 2016-12-02 | One kind extracts concentration systems |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621362229.0U CN206240114U (en) | 2016-12-02 | 2016-12-02 | One kind extracts concentration systems |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206240114U true CN206240114U (en) | 2017-06-13 |
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ID=59007248
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621362229.0U Active CN206240114U (en) | 2016-12-02 | 2016-12-02 | One kind extracts concentration systems |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206240114U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107158729A (en) * | 2017-07-06 | 2017-09-15 | 江苏北松健康产业有限公司 | Concentration systems and alcohol precipitation concentration systems |
| CN107537168A (en) * | 2017-10-19 | 2018-01-05 | 榆林学院 | A kind of regulation and control fixed gas scapus dynamic characteristic promotes the device of steam condensation |
| CN115054983A (en) * | 2022-07-23 | 2022-09-16 | 西安国康瑞金制药有限公司 | A concentrated filtration equipment for preparing intermediate |
-
2016
- 2016-12-02 CN CN201621362229.0U patent/CN206240114U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107158729A (en) * | 2017-07-06 | 2017-09-15 | 江苏北松健康产业有限公司 | Concentration systems and alcohol precipitation concentration systems |
| CN107537168A (en) * | 2017-10-19 | 2018-01-05 | 榆林学院 | A kind of regulation and control fixed gas scapus dynamic characteristic promotes the device of steam condensation |
| CN115054983A (en) * | 2022-07-23 | 2022-09-16 | 西安国康瑞金制药有限公司 | A concentrated filtration equipment for preparing intermediate |
| CN115054983B (en) * | 2022-07-23 | 2024-04-09 | 西安国康瑞金制药有限公司 | A concentrated filtration equipment for preparing medical intermediate |
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