CN206746322U - A kind of refined integrated extraction element of ginger-root extract - Google Patents
A kind of refined integrated extraction element of ginger-root extract Download PDFInfo
- Publication number
- CN206746322U CN206746322U CN201720254296.9U CN201720254296U CN206746322U CN 206746322 U CN206746322 U CN 206746322U CN 201720254296 U CN201720254296 U CN 201720254296U CN 206746322 U CN206746322 U CN 206746322U
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- China
- Prior art keywords
- ginger
- treatment tank
- root extract
- extraction element
- integrated extraction
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Abstract
The utility model provides a kind of refined integrated extraction element of ginger-root extract, it includes treatment tank, membrane filter tube and circulating pump, the treatment tank, membrane filter tube and circulating pump are sequentially connected in series to form the first fluid loop, and treatment tank and circulating pump also connect to form second liquid loop.Compared with prior art, the utility model has following beneficial effect：1st, synchronously complete decolouring, remove solid impurity, microorganism, simplify technique, shorten the process time, improve production efficiency；2nd, operating condition is carried out in normal temperature or relatively low temperature, is advantageous to protect heat-sensitive ingredients not to be destroyed.
Description
Technical field
A kind of refined integrated extraction element of ginger-root extract is the utility model is related to, belongs to natural product extracting technique neck
Domain.
Background technology
In the preparation process of ginger-root extract used for cosmetic, refining and edulcoration is extremely important step, is directly affected
To the stability, security and validity of product, the active carbon decoloring of currently used method, film retention, resin separation, flocculation
Etc. technology, but all there is the defects of some applications, such as process cycle length in these technologies, and loss is big, and cost is high, and use is organic
Reagent etc..Conventional activated carbon stirring removal filtration trouble, the poor selectivity of material；Conventional film retention treatment effeciency is low, film
Flux easily declines；Resin separation costs are high, and need to use organic solvent；Flocculation equally exists filtering and bothered, and just for
The removal of macromolecular substances.
Utility model content
The utility model provides a kind of refined integrated extraction element of ginger-root extract, to solve to be deposited in the prior art
Above mentioned problem.
The utility model is achieved through the following technical solutions：
The utility model provides a kind of refined integrated extraction element of ginger-root extract, and it includes treatment tank, membrane filter tube
And circulating pump, the treatment tank, membrane filter tube and circulating pump are sequentially connected in series to form the first fluid loop, treatment tank and circulating pump are also
Series connection forms second liquid loop.
Use principle of the present utility model is：First fluid loop is used to refine, and second liquid loop is used for independent Carbon fiber
Refining and edulcoration is tieed up, in the first fluid loop, after shedding NACF, can be used for micro-filtration, compressed air passes through air mistake
Filter enters treatment tank, for draining the remaining extract solution in treatment tank.
Race extract solution adds treatment tank from charging aperture, enters membrane filtration by circulating pump after active carbon fibre dimensional filter
Manage, concentrate enters treatment tank through valve and participates in circulating after micro-filtration, and scavenging solution comes out from the lateral of membrane filter tube.
Preferably, the top of the treatment tank is provided with air inlet, and the side wall upper part for the treatment of tank is provided with charging aperture.
Preferably, the outside of the air inlet is provided with air cleaner.
Preferably, the pore size filter of the air cleaner is 0.2~0.45 μm.
Preferably, removably it is filled with NACF in the treatment tank.
Preferably, the pore size filter of the NACF is 10~13nm.
Preferably, the filter medium in the membrane filter tube is ceramic membrane, metal film or PET film.
Preferably, the aperture of the filter medium is 30~200nm.
Compared with prior art, the utility model has following beneficial effect：
1st, synchronously complete and remove solid impurity, microorganism, simplify technique, shorten the process time, improve production efficiency；
2nd, synergy is produced, improves purification efficiency.The concentration of feed liquid is higher during carbon fiber refining and edulcoration, removing it is coloured
Material is more, is constantly removed by scavenging solution in this case, overall density is maintained at higher level, makes removal of impurities more efficient
Progress, if not, need long time to realize refining effect under normal temperature condition, if heating, although can
To shorten Refining times, but the decomposition of heat-sensitive ingredients and the mistake absorption of other active components can be caused；NACF sheet
The filter effect of body and suction-operated constantly pre-process equivalent to before microfiltration membranes to feed liquid, can effectively reduce
Blocking of the feed liquid to film, the decline of membrane flux is reduced, improve integrally refined efficiency；
3rd, operating condition is carried out in normal temperature or relatively low temperature, is advantageous to protect heat-sensitive ingredients not to be destroyed.
Brief description of the drawings
By reading the detailed description made with reference to the following drawings to non-limiting example, other spies of the present utility model
Sign, objects and advantages will become more apparent upon：
Fig. 1 is the structural representation of refining plant in the utility model；
In figure：1st, treatment tank；2nd, membrane filter tube；3rd, circulating pump；4th, air cleaner；5th, valve；11st, charging aperture；12nd, it is living
Property Carbon fibe；13rd, air inlet.
Embodiment
The utility model is described in detail with reference to specific embodiment.Following examples will be helpful to this area
Technical staff further understands the utility model, but does not limit the utility model in any form.It should be pointed out that to ability
For the those of ordinary skill in domain, without departing from the concept of the premise utility, various modifications and improvements can be made.
These belong to the scope of protection of the utility model.
A kind of refining plant of preparation method for foregoing ginger extract provided by the utility model, it includes refined
Tank 1, membrane filter tube 2 and circulating pump 3, treatment tank 1, membrane filter tube 2 and circulating pump 3 are sequentially connected in series to form the first fluid loop, essence
Tank 1 and circulating pump 3 processed, which are also connected, forms second liquid loop, is provided with the first fluid loop and second liquid loop some
Valve 5, a valve 5 is provided with such as between the discharging opening and circulating pump 3 for the treatment of tank 1, between circulating pump 3 and membrane filter tube 2
Provided with a valve 5, a valve 5 is provided between membrane filter tube 2 and treatment tank 1.
The top for the treatment of tank 1 is provided with air inlet 13, and the side wall upper part for the treatment of tank 1 is provided with charging aperture 11.
The outside of air inlet 13 is provided with air cleaner 4, and the pore size filter of air cleaner 4 is 0.2~0.45 μm.
NACF 12 is removably filled with treatment tank 1, the pore size filter of NACF 12 is 10~13nm.
Filter medium in membrane filter tube 2 is ceramic membrane, metal film or PET film, the aperture of filter medium for 30~
200nm。
Described operating condition is：Operation temperature normal temperature~55 DEG C, operating pressure are 0.1~0.3MPa.
Application method of the present utility model is：
By the ginger juice of fresh squeezing, treatment tank is added from charging aperture, film mistake is entered by circulating pump after active carbon fibre dimensional filter
Chimney filter, concentrate enters treatment tank through valve and participates in the ratio between circulation, filter area of active carbon fibre peacekeeping membrane filter tube after micro-filtration
For 2:1, the aperture of NACF is 10nm, and membrane component is 30nm ceramic membranes, and integrated operation pressure is 2kg, and normal temperature condition is smart
During tank feed liquid ＜ 1/2 processed, compressed air enters treatment tank through air cleaner by valve, for draining the remnants in treatment tank
Extract solution, ginger juice scavenging solution is obtained from microfiltration membranes side.
Specific embodiment of the utility model is described above.It is to be appreciated that the utility model not office
It is limited to above-mentioned particular implementation, those skilled in the art can make various deformations or amendments within the scope of the claims,
This has no effect on substantive content of the present utility model.
Claims (8)
1. the refined integrated extraction element of a kind of ginger-root extract, it is characterised in that including treatment tank, membrane filter tube and circulation
Pump, the treatment tank, membrane filter tube and circulating pump are sequentially connected in series to form the first fluid loop, and treatment tank and circulating pump are also connected shape
Into second liquid loop.
2. the refined integrated extraction element of ginger-root extract as claimed in claim 1, it is characterised in that the top of the treatment tank
Portion is provided with air inlet, and the side wall upper part for the treatment of tank is provided with charging aperture.
3. the refined integrated extraction element of ginger-root extract as claimed in claim 2, it is characterised in that outside the air inlet
Side is provided with air cleaner.
4. the refined integrated extraction element of ginger-root extract as claimed in claim 3, it is characterised in that the air cleaner
Pore size filter be 0.2~0.45 μm.
5. the refined integrated extraction element of the ginger-root extract as described in any one in Claims 1 to 4, it is characterised in that
NACF is filled with the treatment tank.
6. the refined integrated extraction element of ginger-root extract as claimed in claim 5, it is characterised in that the NACF
Pore size filter be 10~13nm.
7. the refined integrated extraction element of ginger-root extract as claimed in claim 1, it is characterised in that in the membrane filter tube
Filter medium be ceramic membrane, metal film or PET film.
8. the refined integrated extraction element of ginger-root extract as claimed in claim 7, it is characterised in that the filter medium
Aperture is 30~200nm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720254296.9U CN206746322U (en) | 2017-03-15 | 2017-03-15 | A kind of refined integrated extraction element of ginger-root extract |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720254296.9U CN206746322U (en) | 2017-03-15 | 2017-03-15 | A kind of refined integrated extraction element of ginger-root extract |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206746322U true CN206746322U (en) | 2017-12-15 |
Family
ID=60610164
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720254296.9U Active CN206746322U (en) | 2017-03-15 | 2017-03-15 | A kind of refined integrated extraction element of ginger-root extract |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206746322U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110051603A (en) * | 2019-05-21 | 2019-07-26 | 上海蒂多资国际贸易有限公司 | A kind of preparation method and applications of the compound anti-sensitizer of plant |
-
2017
- 2017-03-15 CN CN201720254296.9U patent/CN206746322U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110051603A (en) * | 2019-05-21 | 2019-07-26 | 上海蒂多资国际贸易有限公司 | A kind of preparation method and applications of the compound anti-sensitizer of plant |
| CN110051603B (en) * | 2019-05-21 | 2021-11-02 | 西安容丽康科技有限公司 | Preparation method and application of plant composite anti-allergy agent |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP02 | Change in the address of a patent holder |
Address after: 201600 rooms 105, 106, 107, 108, 109, 110, 111, 112, 1 / F, building 4, No. 2888, Jiuxin highway, Xinqiao Town, Songjiang District, Shanghai Patentee after: SHANGHAI JIAYU BIOTECHNOLOGY Co.,Ltd. Address before: 201413 Shanghai city four groups in Fengxian District Zhen Ping Gang Road No. 883-885 Building 2 room 1305 Patentee before: SHANGHAI JIAYU BIOTECHNOLOGY Co.,Ltd. |
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| CP02 | Change in the address of a patent holder | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210401 Address after: Room 501, 110 Lane 1351, laohumin Road, Minhang District, Shanghai 201100 Patentee after: Chen Xian Address before: 201600 rooms 105, 106, 107, 108, 109, 110, 111, 112, area C, 1 / F, building 4, 2888, Jiuxin Road, Xinqiao Town, Songjiang District, Shanghai Patentee before: SHANGHAI JIAYU BIOTECHNOLOGY Co.,Ltd. |
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| TR01 | Transfer of patent right |