CN204245047U - The assorted integrating device of a kind of constant temperature water extraction - Google Patents
The assorted integrating device of a kind of constant temperature water extraction Download PDFInfo
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- CN204245047U CN204245047U CN201420595341.3U CN201420595341U CN204245047U CN 204245047 U CN204245047 U CN 204245047U CN 201420595341 U CN201420595341 U CN 201420595341U CN 204245047 U CN204245047 U CN 204245047U
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Abstract
The utility model provides a kind of constant temperature water extraction assorted integrating device, comprises the crushing material module, constant temperature extraction module and the centrifugal module that connect successively; Also comprise one-level UF membrane module, secondary membrane separation module and three grades of UF membrane modules, described centrifugal module connects one-level UF membrane module, secondary membrane separation module and three grades of UF membrane modules simultaneously, and connects quantitative assorted module simultaneously.The utility model by integrated for the process units of tealeaves, and by the cooperation between modules, can look after and guide the grade of the tealeaves of the different quality of height, make different tealeaves can assorted go out identical taste.
Description
Technical field
The utility model relates to a kind of Tea Production device, more specifically, relates to the assorted integrating device of a kind of constant temperature water extraction.
Background technology
The separation and extraction technology of effective content of tea is strategic new and high technology, an important directions is exploitation that is integrated by efficient separating and purifying technology and that equip and production, from natural products, be separated effective ingredient, form the new product of high added value, and can resource utilization be improved.
Effective ingredient contained in tealeaves is the material base determining tealeaves characteristic.Tea tree is the same with other plant, take solar energy as the energy, forms various effective ingredient by a series of vital movement process, determines the panoramic morphological feature of tea tree and value.The coordinating and unifying of effective ingredient in tealeaves, determines tea leaf quality quality and consumption value.After all, the effective ingredient of tealeaves is the material determining the various feature of tealeaves.
Domestic and international scientific research proves, Tea Polyphenols has to be removed human free radical and improve the functions such as immunity, anti-oxidant, anti-ageing, radioresistance, anticancer and reducing blood lipid; Theanine has the function such as hypertensive tranquilizing and improving water flood; Tea polysaccharide has the functions such as hypoglycemic, develop immunitypty; Tea Pigment has the functions such as anticoagulant, antithrombotic and atherosclerosis; Caffeine has cures the function such as asthma and dispelling fatigue.Therefore, the functional component of tealeaves has been widely used in the fields such as medicine, health care and food, and has huge potential market.The functional component of comprehensive exploitation tealeaves is the effective way promoting human health and solve the low and middle-grade tealeaves outlet of China.
The technical approach of existing extraction tealeaves effective ingredient has: (1) hot water extraction, and high-temperature water, as solvent, destroys the composition of tea, the loss of tea fragrance, and the quality of extract is reduced.(2) chemical solvent extracts, and has the residual of chemical substance, reduce the quality of extract in extract.(3) counter-flow extraction, gets by the water extraction of temperature at 80-90 degree, and tea composition is destroyed, and such as, under the long-time condition of high temperature, the loss rate of oxidation of tea effective ingredient will increase, and have impact on the quality of extract.(4) Microwave Extraction, has the residual of chemical solvent, also has the high temperature effective ingredient of tea, reduces the quality of extract.(5) means of supercritical extraction, Main Ingredients and Appearance Tea Polyphenols is insoluble to carbon dioxide, and extraction efficiency is low.(6) freeze drying, respond well, but cost is too high, and be a part of low temperature wherein, walk the effective ingredient loss of Zou before can not ensureing.(7) spraying dry, more than 150 degree, high temperature composition is complete, affects the quality of product.
But at present not the device active ingredient in tealeaves being carried out effectively extract that can be complete.
Utility model content
In order to a step obtain extract in tealeaves, first the utility model provides a kind of constant temperature water extraction assorted integrating device, it is characterized in that, comprises the crushing material module, constant temperature extraction module and the centrifugal module that connect successively; Also comprise one-level UF membrane module, secondary membrane separation module and three grades of UF membrane modules, described centrifugal module connects one-level UF membrane module, secondary membrane separation module and three grades of UF membrane modules simultaneously, and one-level UF membrane module, is interconnected between secondary membrane separation module and three grades of UF membrane modules; The described organic nanofiltration module of one-level UF membrane model calling first and the first concentrate drying module, described secondary membrane separation module connects second organic nanofiltration module and the second concentrate drying module, the 3rd organic nanofiltration module and the 3rd concentrate drying module is all connected with after three grades of described UF membrane modules, the first described concentrate drying module, the second concentrate drying module are connected quantitative assorted module with the 3rd concentrate drying module simultaneously
Described one-level UF membrane module comprises the ceramic membrane that membrane aperture is 0.8-1.2 μm,
Described secondary membrane separation module comprises the ceramic membrane that membrane aperture is 0.1-0.5 μm,
Three grades of described UF membrane modules comprise the ceramic membrane that membrane aperture is 4-50nm.
Described crushing material module comprises for by the high-speed tissue mashing machine of material splitting be used for crushing material to 50 ~ 80 object Universalpulverizer.
It is the centrifuge of more than 3800 that described centrifugal module comprises a rotating speed.
Described organic nanofiltration module comprises organic nanofiltration membrane.
Described irradiation modules comprises inspissator and vacuum drier, the filtrate after nanofiltration is first carried out concentrating and carries out drying again.
Described quantitative assorted module, comprises feeding device and agitating device.
The utility model has the following advantages:
1. device of the present utility model can a stepization operate, and decreases artificial.
2. the vibrational power flow of device of the present utility model is reasonable, by the cooperation of modules, reduces the production time.
3. by device of the present utility model can assorted go out the tealeaves bag of different taste, be applicable to the production of different tealeaves bags, and promote the taste of tealeaves bag.
Accompanying drawing explanation
Fig. 1 is the assorted integrating device schematic diagram of constant temperature water extraction of the present utility model.
Detailed description of the invention
The utility model is further described below in conjunction with the drawings and specific embodiments.Unless stated otherwise, the utility model adopts reagent, equipment and method are conventional commercial reagent, equipment and the conventional method used of the art.
First the utility model provides a kind of constant temperature water extraction assorted integrating device, it is characterized in that, comprises the crushing material module, constant temperature extraction module and the centrifugal module that connect successively; Also comprise one-level UF membrane module, secondary membrane separation module and three grades of UF membrane modules, described centrifugal module connects one-level UF membrane module, secondary membrane separation module and three grades of UF membrane modules simultaneously, and one-level UF membrane module, is interconnected between secondary membrane separation module and three grades of UF membrane modules; The described organic nanofiltration module of one-level UF membrane model calling first and the first concentrate drying module, described secondary membrane separation module connects second organic nanofiltration module and the second concentrate drying module, the 3rd organic nanofiltration module and the 3rd concentrate drying module is all connected with after three grades of described UF membrane modules, the first described concentrate drying module, the second concentrate drying module are connected quantitative assorted module with the 3rd concentrate drying module simultaneously
Described one-level UF membrane module comprises the ceramic membrane that membrane aperture is 0.8-1.2 μm,
Described secondary membrane separation module comprises the ceramic membrane that membrane aperture is 0.1-0.5 μm,
Three grades of described UF membrane modules comprise the ceramic membrane that membrane aperture is 4-50nm.
Described crushing material module comprises for by the high-speed tissue mashing machine of material splitting be used for crushing material to 50 ~ 80 object Universalpulverizer.
It is the centrifuge of more than 3800 that described centrifugal module comprises a rotating speed.
Described organic nanofiltration module comprises organic nanofiltration membrane.
Described irradiation modules comprises inspissator and vacuum drier, the filtrate after nanofiltration is first carried out concentrating and carries out drying again.
Described quantitative assorted module, comprises feeding device and agitating device.
The using method of device of the present utility model is as follows:
First the tealeaves fried is put into crushing material module, 50 ~ 80 object powder are broken into by crushing material module, then constant temperature extraction module is input to by conveyer belt, extracted by constant-temperature hot water, by extract by Cemented filling to centrifugal module, by centrifuge by solid-liquid layering, get liquid layer, and the separation module that selection three kinds is different according to demand, by carrying out organic nanofiltration after separation module, removal heavy metal, then obtain by concentrate drying module the concentrated powder that different membrane aperture filters gained, according to seeking, by assorted according to a certain percentage for different concentrated powder, by a certain percentage concentrated powder is joined in feeding device, by the agitating device of quantitative assorted module, mixing, finally pack, obtain a kind of tealeaves condensed powders.
Claims (6)
1. the assorted integrating device of constant temperature water extraction, is characterized in that, comprises the crushing material module, constant temperature extraction module and the centrifugal module that connect successively; Also comprise one-level UF membrane module, secondary membrane separation module and three grades of UF membrane modules, described centrifugal module connects one-level UF membrane module, secondary membrane separation module and three grades of UF membrane modules simultaneously, and one-level UF membrane module, is interconnected between secondary membrane separation module and three grades of UF membrane modules; The described organic nanofiltration module of one-level UF membrane model calling first and the first concentrate drying module, described secondary membrane separation module connects second organic nanofiltration module and the second concentrate drying module, the 3rd organic nanofiltration module and the 3rd concentrate drying module is all connected with after three grades of described UF membrane modules, the first described concentrate drying module, the second concentrate drying module are connected quantitative assorted module with the 3rd concentrate drying module simultaneously
Described one-level UF membrane module comprises the ceramic membrane that membrane aperture is 0.8-1.2 μm,
Described secondary membrane separation module comprises the ceramic membrane that membrane aperture is 0.1-0.5 μm,
Three grades of described UF membrane modules comprise the ceramic membrane that membrane aperture is 4-50nm.
2. the assorted integrating device of constant temperature water extraction according to claim 1, is characterized in that, described crushing material module comprises for by the high-speed tissue mashing machine of material splitting be used for crushing material to 50 ~ 80 object Universalpulverizer.
3. the assorted integrating device of constant temperature water extraction according to claim 1, is characterized in that, it is the centrifuge of more than 3800 that described centrifugal module comprises a rotating speed.
4. the assorted integrating device of constant temperature water extraction according to claim 1, is characterized in that, described organic nanofiltration module comprises organic nanofiltration membrane.
5. the assorted integrating device of constant temperature water extraction according to claim 1, it is characterized in that, described irradiation modules comprises inspissator and vacuum drier, the filtrate after nanofiltration is first carried out concentrating and carries out drying again.
6. the assorted integrating device of constant temperature water extraction according to claim 1, is characterized in that, described quantitative assorted module, comprises feeding device and agitating device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420595341.3U CN204245047U (en) | 2014-10-15 | 2014-10-15 | The assorted integrating device of a kind of constant temperature water extraction |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420595341.3U CN204245047U (en) | 2014-10-15 | 2014-10-15 | The assorted integrating device of a kind of constant temperature water extraction |
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| Publication Number | Publication Date |
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| CN204245047U true CN204245047U (en) | 2015-04-08 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420595341.3U Expired - Fee Related CN204245047U (en) | 2014-10-15 | 2014-10-15 | The assorted integrating device of a kind of constant temperature water extraction |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105104590A (en) * | 2015-08-21 | 2015-12-02 | 中国农业科学院茶叶研究所 | Tea flavor quality component food directional manufacturing technology integration system and method |
| WO2016201706A1 (en) * | 2015-06-19 | 2016-12-22 | 广东正源华茶生物股份有限公司 | Plant molecular purification technique integration system |
-
2014
- 2014-10-15 CN CN201420595341.3U patent/CN204245047U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016201706A1 (en) * | 2015-06-19 | 2016-12-22 | 广东正源华茶生物股份有限公司 | Plant molecular purification technique integration system |
| CN105104590A (en) * | 2015-08-21 | 2015-12-02 | 中国农业科学院茶叶研究所 | Tea flavor quality component food directional manufacturing technology integration system and method |
| CN105104590B (en) * | 2015-08-21 | 2019-08-13 | 中国农业科学院茶叶研究所 | Tealeaves flavor quality component foodization orientation manufacture Integration ofTechnology system and method |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150408 Termination date: 20171015 |
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| CF01 | Termination of patent right due to non-payment of annual fee |