CN205627641U - Enrichment facility for extract product - Google Patents

Enrichment facility for extract product Download PDF

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Publication number
CN205627641U
CN205627641U CN201620392991.7U CN201620392991U CN205627641U CN 205627641 U CN205627641 U CN 205627641U CN 201620392991 U CN201620392991 U CN 201620392991U CN 205627641 U CN205627641 U CN 205627641U
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China
Prior art keywords
conveyance conduit
storage tank
membrance concentration
pipeline
control valve
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CN201620392991.7U
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Chinese (zh)
Inventor
李汁
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Yunnan Benefit Biotechnology Co Ltd
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Yunnan Benefit Biotechnology Co Ltd
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Priority to CN201620392991.7U priority Critical patent/CN205627641U/en
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Abstract

The utility model provides an enrichment facility for extract product, including the storage tank of taking first feed inlet, the concentrated subassembly of membrane, the permeate liquid collection tank, be equipped with a pipeline between the concentrated subassembly inlet of storage tank discharge gate and membrane, be equipped with the 2nd pipeline between the concentrated subassembly liquid outlet of storage tank second feed inlet and membrane, be equipped with the 3rd pipeline between concentrated subassembly permeate liquid export of membrane and the permeate liquid collection tank, be equipped with the cooler on the pipeline of its characterized in that between storage tank liquid outlet and the concentrated subassembly inlet of membrane, and set up the fourth pipeline who takes the first control valve between the 2nd pipeline and a pipeline, be equipped with the second control valve on being close to the 2nd pipeline of storage tank second feed inlet. When messenger's extract carried out the physics concentration under low temperature environment, effective removal of solvent, inorganic salts, heavy metal etc. Improved concentration efficiency and yield, reduce energy consumption.

Description

A kind of extract enrichment facility
Technical field
This utility model relates to a kind of enrichment facility, particularly a kind of extract enrichment facility, belongs to biochemical industry extraction equipment design and manufacturing technology field.
Background technology
Effective ingredients in plant, especially Radix Notoginseng active ingredient extraction in, conventional dissolubility ethanol good, lower boiling extracts, in order to the active ingredient dissolved, isolate in Radix Notoginseng, afterwards while concentration and recovery ethanol, obtains high-purity Radix Notoginseng extract.Existing concentration uses steam heat concentrator to complete mostly, owing to needing heating when concentrating, not only energy consumption is higher, and steam heat concentrates and is also easy to damage the thermo-responsive composition in Radix Notoginseng extract, reduce yield, increase cost, with intermittent fever concentration process has only evaporated alcohol solvent, some inorganic salts, heavy metal but can not get effectively removing, and finally affect the quality of extract.It is therefore desirable to prior art is improved.
Summary of the invention
Energy consumption height is there is for solving existing steam heat concentrator, thermo-responsive composition in extract is damaged, reduce yield, increase cost, with intermittent fever concentration process has only evaporated solvent, the problems such as some inorganic salts, heavy metal but can not get effectively removing, the final quality affecting extract, this utility model provides a Plant Extracts enrichment facility.
nullThis utility model is completed by following technical proposal: a kind of extract enrichment facility,Including the storage tank with the first charging aperture、Membrance concentration assembly、Permeate collecting tank,It is provided with the first conveyance conduit between storage tank discharging opening and membrance concentration assembly inlet,It is provided with the second conveyance conduit between storage tank the second charging aperture and membrance concentration assembly liquid outlet,It is provided with the 3rd conveyance conduit between the outlet of membrance concentration assembly permeate and permeate collecting tank,It is characterized in that being provided with cooler on the first conveyance conduit between storage tank liquid outlet and membrance concentration assembly inlet,And the 4th conveyance conduit with the first control valve is set between the second conveyance conduit and the first conveyance conduit,It is being provided with the second control valve on the second conveyance conduit of storage tank the second charging aperture,With by the first conveyance conduit by before extract transport membrane thickening apparatus,After first passing through cooler reduction extract temperature,Carry out membrance concentration again,While allowing extract concentrate at low ambient temperatures,Make solvent、Inorganic salt、Heavy metals etc. are by effectively through in rear entrance permeate collecting tank,Available solvent is reclaimed after postorder processes,Concentrate then returns fluid reservoir or again carries out membrance concentration through the 4th conveyance conduit,Finally give high-quality concentrate,Realize extracting solution low-power consumption、Low-temperature physics circulation concentrates,Effectively remove the inorganic salt in extract、Heavy metal,Ensure that extract active ingredient is not lost.
Described membrance concentration assembly is concentrated part by the Multistage Membranes being sequentially connected with and forms, wherein inlet and first conveyance conduit of first order membrance concentration part is connected, the liquid outlet of afterbody membrance concentration part and second and the 4th conveyance conduit be connected, the permeate outlet of membrance concentration parts at different levels is all connected with permeate collecting tank by the 3rd conveyance conduit and the 3rd control valve, will pass through multistage concentration, the solvent that will transmit through, inorganic salt, heavy metal sends into the recycling of permeate collecting tank, and eliminate solvent, inorganic salt, the concentrate of heavy metal then returns storage tank or feeding membrance concentration assembly concentrates again.
Described first conveyance conduit is provided with the 4th control valve and drainage conduit, in order to sent by concentrate.
Described first conveyance conduit is provided with liquid pump and booster pump, in order to is sent in cooler by the extracting solution in storage tank by liquid pump, is re-fed in membrance concentration assembly;Or by booster pump, the concentrated solution that membrance concentration assembly is discharged is fed again in cooler, membrance concentration assembly circulation to concentrate.
Described first conveyance conduit is connected with the 5th conveyance conduit with the 5th control valve on it by threeway, and the 5th conveyance conduit is connected with the cleaning fluid tank of tape entry, to need to be carried out cooler, membrance concentration assembly, storage tank according to production.
Described cooler is plate type heat exchanger, in order to extracting solution is carried out heat exchange cooling.
Described control valve, liquid pump, booster pump are connected with peripheral control unit by wire respectively, in order to regulated and controled whole device by controller.
This utility model has following advantages and effect: use such scheme; can be conveniently by cooler and the setting of membrance concentration assembly; while making extracting solution carry out physical concentration at low ambient temperatures; solvent, inorganic salt, heavy metal etc. is made to be efficiently removed; while improving thickening efficiency, protecting effective ingredient not lose, reduce energy resource consumption.The most also can need carry out local circulation or all circulate concentration according to production, condensing mode is flexible, controlled, it is ensured that concentrate quality.Again by the setting of cleaning fluid tank, whole concentration systems can be cleared up automatically, it is ensured that persistently carrying out of production.An actually preferable enrichment facility.
Accompanying drawing explanation
Fig. 1 is the structure chart of this utility model.
Detailed description of the invention
Below in conjunction with the accompanying drawings this utility model is further described.
The extract enrichment facility that this utility model provides, including the storage tank 1 with the first charging aperture 2, membrance concentration assembly 7, permeate collecting tank 10, the first conveyance conduit 15 it is provided with between storage tank 1 discharging opening and membrance concentration assembly 7 inlet, the second conveyance conduit 4 it is provided with between storage tank 1 second charging aperture 3 and membrance concentration assembly 7 liquid outlet, it is provided with the 3rd conveyance conduit 8 between the outlet of membrance concentration assembly 7 permeate and permeate collecting tank 10, it is provided with cooler 11 on the first conveyance conduit 15 between storage tank 1 liquid outlet and membrance concentration assembly 7 inlet, and the 4th conveyance conduit 13 with the first control valve 6 is set between the second conveyance conduit 4 and the first conveyance conduit 15, it is being provided with the second control valve 5 on the second conveyance conduit 4 of storage tank 1 second charging aperture 3;Described membrance concentration assembly 7 is made up of the three grades of membrance concentration parts being sequentially connected with, wherein inlet and first conveyance conduit 15 of first order membrance concentration part is connected, the liquid outlet of afterbody membrance concentration part and second and the 4th conveyance conduit 4, 13 are connected, the permeate outlet of membrance concentration parts at different levels is all connected with permeate collecting tank 10 by the 3rd conveyance conduit 8 and the 3rd control valve 9, will pass through multistage concentration, the solvent that will transmit through, inorganic salt, heavy metal is sent into permeate collecting tank 10 and is recycled, and eliminate solvent, inorganic salt, the concentrate of heavy metal then returns storage tank 1 or feeding membrance concentration assembly 7 concentrates again;Described first conveyance conduit 15 is provided with the 4th control valve 21 and drainage conduit 20, in order to sent by concentrate;Described first conveyance conduit 15 is provided with liquid pump 14 and booster pump 12, in order to is sent in cooler 11 by the extracting solution in storage tank 1 by liquid pump 14, is re-fed in membrance concentration assembly 7;Or by booster pump 12, the concentrated solution that membrance concentration assembly 7 is discharged is fed again in cooler 11, membrance concentration assembly 7 circulation to concentrate;Described first conveyance conduit 15 is connected with the 5th conveyance conduit 16 with the 5th control valve 17 on it by threeway, 5th conveyance conduit 16 is connected with the cleaning fluid tank 18 of tape entry 19, to need to be carried out cooler 11, membrance concentration assembly 7, storage tank 1 etc. according to production;Described cooler 11 is conventional plate type heat exchanger, in order to extracting solution is carried out heat exchange cooling;Each control valve described, liquid pump 14, booster pump 12 are connected with peripheral control unit by wire respectively, in order to regulated and controled whole device by controller.
During work, first extract is transported to after cooler 11 lowers the temperature by the first conveyance conduit 15, it is re-fed into membrance concentration assembly 7 and carries out membrance concentration, while allowing extract concentrate at low ambient temperatures, make solvent, inorganic salt, after the tunicle thickening apparatus 7 such as heavy metal effectively pass through, enter in permeate collecting tank 10, available solvent is reclaimed after postorder processes, concentrate then returns fluid reservoir 1 or again carries out membrance concentration through the 4th conveyance conduit 13, send through drainage conduit 20 after finally giving high-quality concentrate, realize extracting solution low-power consumption, low-temperature physics circulation concentrates, effectively remove the inorganic salt in extract, heavy metal, ensure that extract active ingredient is not lost.When device is carried out by needs, the cleanout fluid in cleaning fluid tank 18 is sent into the first conveyance conduit 15, cooler 11 through the 5th conveyance conduit 16, membrance concentration assembly the 7, the 3rd conveyance conduit 8, second carries pipe the 4, the 4th conveyance conduit 6, storage tank 1 is carried out.

Claims (5)

1. an extract enrichment facility, including the storage tank with the first charging aperture, membrance concentration assembly, permeate collecting tank, it is provided with the first conveyance conduit between storage tank discharging opening and membrance concentration assembly inlet, it is provided with the second conveyance conduit between storage tank the second charging aperture and membrance concentration assembly liquid outlet, it is provided with the 3rd conveyance conduit between the outlet of membrance concentration assembly permeate and permeate collecting tank, it is characterized in that being provided with cooler on the first conveyance conduit between storage tank liquid outlet and membrance concentration assembly inlet, and the 4th conveyance conduit with the first control valve is set between the second conveyance conduit and the first conveyance conduit, it is being provided with the second control valve on the second conveyance conduit of storage tank the second charging aperture.
Extract enrichment facility the most according to claim 1, it is characterized in that described membrance concentration assembly is concentrated part by the Multistage Membranes being sequentially connected with and forms, wherein inlet and first conveyance conduit of first order membrance concentration part is connected, the liquid outlet of afterbody membrance concentration part and second and the 4th conveyance conduit be connected, the outlet of the permeate of membrance concentration parts at different levels is all connected with permeate collecting tank by the 3rd conveyance conduit and the 3rd control valve.
Extract enrichment facility the most according to claim 1, it is characterised in that described first conveyance conduit is provided with the 4th control valve and drainage conduit.
Extract enrichment facility the most according to claim 1, it is characterised in that described first conveyance conduit is provided with liquid pump and booster pump.
Extract enrichment facility the most according to claim 1, it is characterised in that described first conveyance conduit is connected with the 5th conveyance conduit with the 5th control valve on it by threeway, and the 5th conveyance conduit is connected with the cleaning fluid tank of tape entry.
CN201620392991.7U 2016-05-04 2016-05-04 Enrichment facility for extract product Active CN205627641U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620392991.7U CN205627641U (en) 2016-05-04 2016-05-04 Enrichment facility for extract product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620392991.7U CN205627641U (en) 2016-05-04 2016-05-04 Enrichment facility for extract product

Publications (1)

Publication Number Publication Date
CN205627641U true CN205627641U (en) 2016-10-12

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Application Number Title Priority Date Filing Date
CN201620392991.7U Active CN205627641U (en) 2016-05-04 2016-05-04 Enrichment facility for extract product

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109865431A (en) * 2017-12-01 2019-06-11 广州中国科学院先进技术研究所 A kind of film integrating device and protein matter separation method for protein matter separation concentration

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109865431A (en) * 2017-12-01 2019-06-11 广州中国科学院先进技术研究所 A kind of film integrating device and protein matter separation method for protein matter separation concentration

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