CN207062182U - A kind of algal polysaccharides extract solution enrichment facility - Google Patents
A kind of algal polysaccharides extract solution enrichment facility Download PDFInfo
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- CN207062182U CN207062182U CN201720975365.5U CN201720975365U CN207062182U CN 207062182 U CN207062182 U CN 207062182U CN 201720975365 U CN201720975365 U CN 201720975365U CN 207062182 U CN207062182 U CN 207062182U
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Abstract
Enrichment facility technical field is the utility model is related to, more particularly to a kind of algal polysaccharides extract solution enrichment facility.Including fluid reservoir, filter, reactor, air blower, drying device, collecting tank, condensing unit and negative pressure pump, the reactor inner top is provided with moisture absorption apparatus, link is provided with the reactor inner bottom part, the end set of the link has ultrasonic oscillator, and heater is provided with the madial wall of the reactor.The enrichment facility is simple in construction, and principle is understandable, as the algal polysaccharides of vapor evaporation are reclaimed, can will effectively increase the utilization rate of algal polysaccharides when distilling, practical, is adapted to promote in this area.
Description
Technical field
Enrichment facility technical field is the utility model is related to, more particularly to a kind of algal polysaccharides extract solution enrichment facility.
Background technology
Marine alga is the important component of living marine resources, is broadly divided into blue-green algae, green alga, red algae and brown alga, at present should
It is mainly brown alga, red algae and green alga with relatively broad marine alga, mainly turns into the mankind in the important of food, industry and medicinal aspect
Source.Containing abundant polysaccharide in marine alga, algal polysaccharides be by multiple identical or different monosaccharide groups by glycosidic bond be connected and
Into polymeric carbohydrate, algal polysaccharides are essentially from sea-tangle, deer's tail dish (sargassum fusifome), bulk kelp, yellow tang, bladder-wrack etc.
Marine alga, algal polysaccharides mainly include algin, fucoidin and laminaran, have very high application value, such as agar, OK a karaoke club
Glue, alginic acid etc. are industrially long-term use of.In addition, algal polysaccharides have multiple biological activities and medical value, it is such as disease-resistant
Poison, immunological regulation, antitumor, anticoagulation, anti-oxidant etc..Therefore, the extraction of algal polysaccharides and concentration technique are increasingly by weight
Depending on, the concentration technique of existing algal polysaccharides, it is exactly often to be distilled algal polysaccharides extract solution, finally obtains concentrate, by
It is larger in solubility of the algal polysaccharides in water, so occurring that algal polysaccharides evaporate together with vapor when distillation
The phenomenon fallen, and algal polysaccharides are easily destroyed in high-temperature steam, cause the waste of resource, therefore, a kind of new sea
The enrichment facility of polysaccharides extract solution needs to be invented.
Utility model content
In view of the foregoing, it is necessary to which a kind of algal polysaccharides extract solution enrichment facility is provided.
To reach above-mentioned purpose, technical scheme is used by the utility model：
A kind of algal polysaccharides extract solution enrichment facility, including fluid reservoir, reactor, air blower, collecting tank and negative pressure pump, institute
State reactor inner top and be provided with moisture absorption apparatus, link, the end of the link are provided with the reactor inner bottom part
Be provided with ultrasonic oscillator, be provided with heater on the madial wall of the reactor, the fluid reservoir by connecting tube with
The upper end connection of the reactor, the air outlet of the air blower is connected by connecting tube with the bottom of the reactor, described
Fluid reservoir is connected by connecting tube with the moisture absorption apparatus, and the negative pressure pump is located at the company of the fluid reservoir and the moisture absorption apparatus
In adapter, negative pressure direction caused by the negative pressure pump is to be passed through by the moisture absorption apparatus towards the fluid reservoir, the collecting tank
Connecting tube connects with the lower end of the reactor.
Further, the device also includes filter, and the filter is located at the fluid reservoir and the reactor
Between connecting tube on.
Further, it is provided with liquid flowing valve in the connecting tube between the fluid reservoir and the filter.
Further, the device also includes drying device, and the drying device is located at the air blower and the reactor
Between connecting tube on.
Further, the drying device in the connecting tube of the reactor with being provided with one-way cock, the check valve
The direction of door is towards the reactor by the drying device.
Further, the device also includes condensing unit, and the condensing unit is located at the negative pressure pump and filled with the moisture absorption
In connecting tube between putting.
Further, liquid valve door is provided with the connecting tube between the reactor and the collecting tank.
The utility model has the advantages that：
1st, algal polysaccharides extract solution enrichment facility of the present utility model, the extract solution in fluid reservoir enter in reactor
Row distillation, under the dual cooperation using heating arrangements and ultrasonic oscillator, can allow extract solution to be brought rapidly up, and then can add
Fast distillation speed, and ultrasonic oscillator also acts the effect of stirring so that extract solution is heated evenly, and further prevents marine alga
Polysaccharide component is taken away by vapor, makes distillation more abundant, while under the double action of air blower and negative pressure pump, distillation produces
Vapor movement velocity accelerate, vapor can drive a small amount of algal polysaccharides to enter in moisture absorption apparatus, and then enter
Liquid is liquefied as in condensing unit, algal polysaccharides composition is avoided and is contacted for a long time with high-temperature steam and destroyed, liquid is in negative pressure
It can be returned in fluid reservoir in the presence of pump and re-start distillation preparation next time.
2nd, algal polysaccharides extract solution enrichment facility of the present utility model, simple in construction, principle is understandable, can by distillation when with
The algal polysaccharides composition of dampening evaporation of vapours is reclaimed, and effectively increases the utilization rate of algal polysaccharides, practical, is adapted to
Promote this area.
The utility model be applied to Chinese invention patent application CN201610455239, CN201610108388,
Extraction and/or concentration about composition in CN201610069242 and CN201710204665.
Brief description of the drawings
Fig. 1 is the connection diagram of the utility model algal polysaccharides extract solution enrichment facility；
Fig. 2 is the internal structure schematic diagram of the utility model reactor.
Main element symbol description：
In figure：Fluid reservoir 1, filter 2, reactor 3, air blower 4, drying device 5, collecting tank 6, condensing unit 7, bear
Press pump 8, moisture absorption apparatus 9, link 10, ultrasonic oscillator 11, heater 12, liquid flowing valve 13, one-way cock 14, go out liquid
Valve 15.
Following embodiment will further illustrate the utility model with reference to above-mentioned accompanying drawing.
Embodiment
Fig. 1 and Fig. 2 are referred to, in a kind of better embodiment of the present utility model, a kind of algal polysaccharides extract solution is dense
Compression apparatus, including fluid reservoir 1, filter 2, reactor 3, air blower 4, drying device 5, collecting tank 6, condensing unit 7 and negative
Press pump 8, the inner top of reactor 3 is provided with moisture absorption apparatus 9, link 10 is provided with the inner bottom part of reactor 3, described
The end set of link 10 has ultrasonic oscillator 11, and heater 12 is provided with the madial wall of the reactor 3；It is described
Fluid reservoir 1 is connected by connecting tube with the upper end of the reactor 3, the filter 2 be located at the fluid reservoir 1 with it is described anti-
Answer in the connecting tube between kettle 3, liquid flowing valve 13 is provided with the connecting tube between the fluid reservoir 1 and the filter 2；
The air outlet of the air blower 4 is connected by connecting tube with the bottom of the reactor 3, and the drying device 5 is located at the drum
In connecting tube between blower fan 4 and the reactor 3, set in the connecting tube between the drying device 5 and the reactor 3
There is an one-way cock 14, the direction of the one-way cock 14 is towards the reactor 3 by the drying device 5；The fluid reservoir 1
Connected by connecting tube with the moisture absorption apparatus 9, the negative pressure pump 8 is located at the connection of the fluid reservoir 1 and the moisture absorption apparatus 9
Guan Shang, negative pressure direction caused by the negative pressure pump 8 are towards the fluid reservoir 1, the condensing unit 7 by the moisture absorption apparatus 9
In connecting tube between the negative pressure pump 8 and the moisture absorption apparatus 9；The collecting tank 6 passes through connecting tube and the reaction
The lower end of kettle 3 is connected, and liquid valve door 15 is provided with the connecting tube between the reactor 3 and the collecting tank 6.
Operation principle：Algal polysaccharides extract solution is added in the fluid reservoir 1, opens the liquid flowing valve 13, extract solution
The filter 2 can be flowed through along connecting tube to eventually enter into the reactor 3, start the ultrasonic oscillator 11 and institute
Heater 12 is stated, extract solution is heated under double action, moisture starts to evaporate, and then starts the air blower 4, the negative pressure
Pump 8, the moisture absorption apparatus 9, under three's collective effect, vapor is set to quickly enter condensation dress with the algal polysaccharides inside vapor
Put and be liquefied as liquid, avoid algal polysaccharides and mixed for a long time with high-temperature vapor, reduce the possibility by high temperature
Property, liquid eventually returns in the fluid reservoir 1 along connecting tube, has reclaimed the algal polysaccharides in steam, improved raw material
Utilization rate, after distillation terminates, the ultrasonic oscillator 11 and the heater 12 are closed, simultaneously closes off the negative pressure pump 8
With the moisture absorption apparatus 9, continue to retain the air blower 4 to concentrate progress air blast cooling work, concentrate is quickly cooled down
To normal temperature, the air blower 4 is finally closed, opens the liquid valve door 15 so that concentrate eventually enters into the collecting tank 6
In, enriching service terminates.The enrichment facility is simple in construction, and principle is understandable, the marine alga that will can be evaporated during distillation with vapor
Polysaccharide is reclaimed, and effectively increases the utilization rate of algal polysaccharides, practical, is adapted to promote in this area.
Described above is the detailed description for the preferable possible embodiments of the utility model, but embodiment is not limited to
Patent claim of the present utility model, the equal change or modification completed under the technical spirit suggested by all the utility model
Change, all should belong to the utility model and cover the scope of the claims.
Claims (7)
- A kind of 1. algal polysaccharides extract solution enrichment facility, it is characterised in that：Including fluid reservoir, reactor, air blower, collecting tank and Negative pressure pump, the reactor inner top are provided with moisture absorption apparatus, link, the connection are provided with the reactor inner bottom part The end set of frame has ultrasonic oscillator, and heater is provided with the madial wall of the reactor, and the fluid reservoir passes through Connecting tube is connected with the upper end of the reactor, and the air outlet of the air blower is connected by the bottom of connecting tube and the reactor Logical, the fluid reservoir is connected by connecting tube with the moisture absorption apparatus, and the negative pressure pump is located at the fluid reservoir and the moisture absorption In the connecting tube of device, negative pressure direction caused by the negative pressure pump is towards the fluid reservoir, the receipts by the moisture absorption apparatus Collection tank is connected by connecting tube with the lower end of the reactor.
- A kind of 2. algal polysaccharides extract solution enrichment facility according to claim 1, it is characterised in that：Also include filtering dress Put, the filter is in the connecting tube between the fluid reservoir and the reactor.
- A kind of 3. algal polysaccharides extract solution enrichment facility according to claim 2, it is characterised in that：The fluid reservoir and institute State and be provided with liquid flowing valve in the connecting tube between filter.
- A kind of 4. algal polysaccharides extract solution enrichment facility according to claim 1, it is characterised in that：Also include drying dress Put, the drying device is in the connecting tube between the air blower and the reactor.
- A kind of 5. algal polysaccharides extract solution enrichment facility according to claim 4, it is characterised in that：The drying device with One-way cock is provided with the connecting tube of the reactor, the direction of the one-way cock is as described in drying device direction Reactor.
- A kind of 6. algal polysaccharides extract solution enrichment facility according to claim 1, it is characterised in that：Also include condensation dress Put, the condensing unit is in the connecting tube between the negative pressure pump and the moisture absorption apparatus.
- A kind of 7. algal polysaccharides extract solution enrichment facility according to claim 1, it is characterised in that：The reactor and institute State and liquid valve door is provided with the connecting tube between collecting tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720975365.5U CN207062182U (en) | 2017-08-07 | 2017-08-07 | A kind of algal polysaccharides extract solution enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720975365.5U CN207062182U (en) | 2017-08-07 | 2017-08-07 | A kind of algal polysaccharides extract solution enrichment facility |
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| Publication Number | Publication Date |
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| CN207062182U true CN207062182U (en) | 2018-03-02 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109091047A (en) * | 2018-07-19 | 2018-12-28 | 北京小米移动软件有限公司 | Hand washing machine goes out hydraulic control method, apparatus and storage medium |
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2017
- 2017-08-07 CN CN201720975365.5U patent/CN207062182U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109091047A (en) * | 2018-07-19 | 2018-12-28 | 北京小米移动软件有限公司 | Hand washing machine goes out hydraulic control method, apparatus and storage medium |
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