CN209549439U - The preparation facilities of phase double emulsion gel in a kind of DHA algal oil is high - Google Patents
The preparation facilities of phase double emulsion gel in a kind of DHA algal oil is high Download PDFInfo
- Publication number
- CN209549439U CN209549439U CN201822006645.2U CN201822006645U CN209549439U CN 209549439 U CN209549439 U CN 209549439U CN 201822006645 U CN201822006645 U CN 201822006645U CN 209549439 U CN209549439 U CN 209549439U
- Authority
- CN
- China
- Prior art keywords
- magnetic ball
- ball impact
- impact chamber
- micro
- phase
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000000839 emulsion Substances 0.000 title claims abstract description 36
- 238000002360 preparation method Methods 0.000 title claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 238000002347 injection Methods 0.000 claims abstract description 19
- 239000007924 injection Substances 0.000 claims abstract description 19
- 238000003860 storage Methods 0.000 abstract description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 2
- 229910052760 oxygen Inorganic materials 0.000 abstract description 2
- 239000001301 oxygen Substances 0.000 abstract description 2
- 239000012071 phase Substances 0.000 description 54
- 235000019198 oils Nutrition 0.000 description 30
- 239000007788 liquid Substances 0.000 description 27
- 239000008346 aqueous phase Substances 0.000 description 18
- 239000006210 lotion Substances 0.000 description 12
- 239000000499 gel Substances 0.000 description 9
- 108010046377 Whey Proteins Proteins 0.000 description 6
- 102000007544 Whey Proteins Human genes 0.000 description 6
- 235000021119 whey protein Nutrition 0.000 description 6
- 230000009471 action Effects 0.000 description 5
- 239000012530 fluid Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- 229960003681 gluconolactone Drugs 0.000 description 4
- 229940094952 green tea extract Drugs 0.000 description 4
- 235000020688 green tea extract Nutrition 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 3
- 108010010803 Gelatin Proteins 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- 239000003651 drinking water Substances 0.000 description 3
- 235000020188 drinking water Nutrition 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000008273 gelatin Substances 0.000 description 3
- 229920000159 gelatin Polymers 0.000 description 3
- 235000019322 gelatine Nutrition 0.000 description 3
- 235000011852 gelatine desserts Nutrition 0.000 description 3
- 239000004519 grease Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- WBHHMMIMDMUBKC-QJWNTBNXSA-M ricinoleate Chemical compound CCCCCC[C@@H](O)C\C=C/CCCCCCCC([O-])=O WBHHMMIMDMUBKC-QJWNTBNXSA-M 0.000 description 3
- 229940066675 ricinoleate Drugs 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 241000195493 Cryptophyta Species 0.000 description 2
- PHOQVHQSTUBQQK-SQOUGZDYSA-N D-glucono-1,5-lactone Chemical compound OC[C@H]1OC(=O)[C@H](O)[C@@H](O)[C@@H]1O PHOQVHQSTUBQQK-SQOUGZDYSA-N 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 238000003475 lamination Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 235000019476 oil-water mixture Nutrition 0.000 description 2
- 230000001953 sensory effect Effects 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 244000269722 Thea sinensis Species 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 235000006708 antioxidants Nutrition 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000013270 controlled release Methods 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 239000006071 cream Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 235000009569 green tea Nutrition 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 235000018102 proteins Nutrition 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000008685 targeting Effects 0.000 description 1
Landscapes
- Medicines Containing Material From Animals Or Micro-Organisms (AREA)
Abstract
The utility model provides the preparation facilities of phase double emulsion gel in a kind of DHA algal oil height, including oily phase feed inlet, micro- magnetic ball impact chamber, magnetic ball impact chamber, discharge port and the first, second water phase injection port；The oil phase feed inlet, the first water phase injection port are connected to the side of micro- magnetic ball impact chamber respectively, and the other side of micro- magnetic ball impact chamber is connected to the magnetic ball impact chamber, and the second water phase injection port is connected to the magnetic ball impact chamber；Micro- magnetic ball impact chamber and magnetic ball impact chamber are all set in alternating magnetic field, and micro- magnetic ball impact chamber and the intracavitary portion of magnetic ball impact are equipped with several magnetic balls.The utility model can realize the continuous preparation of phase " w/o/w " double emulsion gel in DHA algal oil height, product stability is good, it also can obviously improve the unstable phenomenons such as bleed, the condensate oil in high fat liquor storage, DHA algal oil is locked in internal cavities, reduction system oxygen content promotes product stability performance.
Description
Technical field
The utility model belongs to double emulsion technical field, and in particular to phase double emulsion gel in a kind of DHA algal oil is high
Preparation facilities.
Background technique
Double emulsion is the highly structural fluid that more droplet is wrapped in a kind of dispersed phase drop, is broadly divided into W/O/
W type and O/W/O type.Double emulsion can be used as carrier, is isolated, protected and controlled release to drug, active constituent, in agriculture
The industries such as industry, food, medical treatment and cosmetics have obtained extensive utilization.
High Internal Phase Emulsion refers to a kind of lotion of the dispersed phase volume fraction 74% or more.The body of dispersed phase in ordinary emulsion
Fraction is generally 30-40%, highest to reach 50%.Dispersed phase drop is dispersed in continuous phase with mutual disjunct spherical shape.
If continuing growing the volume fraction of dispersed phase, when the tightly packed spherical shape at interconnection of dispersed phase drop, at this time
Dispersed phase volume fraction is 74%.Dispersed phase volume fraction is further increased, will occur to squeeze mutually between drop, Zhi Daokong
Between maximum saturation, formed High Internal Phase Emulsion.
The preparation process of double emulsion and High Internal Phase Emulsion is more mature, however, being restricted by many factors, phase in height
Double emulsion is also difficult to prepare, and crucial core equipment is also badly in need of developing.
Utility model content
For phase double emulsion in current height preparation it is more difficult the problems such as, the utility model is provided in a kind of DHA algal oil height
The preparation facilities of phase double emulsion gel.
The utility model discloses a kind of preparation facilities of phase double emulsion gel in DHA algal oil height, including oil mutually to feed
Mouth, micro- magnetic ball impact chamber, magnetic ball impact chamber, discharge port and the first, second water phase injection port；The oil phase feed inlet, first
Water phase injection port is connected to the side of micro- magnetic ball impact chamber respectively, the other side of micro- magnetic ball impact chamber and the magnetic ball
Impact cavity connection, the second water phase injection port are connected to the magnetic ball impact chamber；Micro- magnetic ball impact chamber and magnetic ball impact
Chamber is all set in alternating magnetic field, and micro- magnetic ball impact chamber and the intracavitary portion of magnetic ball impact are equipped with several magnetic balls.
The diameter of the intracavitary magnetic ball of micro- magnetic ball impact is equal；The magnetic ball that the intracavitary portion of the magnetic ball impact is placed be two kinds not
Same diameter.
Compared with prior art, the beneficial effects of the utility model are shown:
1, the utility model is crosslinked whey protein isolate by calcium carbonate-gluconolactone, is aided with dynamic magnetic ball impact skill
Art prepares lotion, so that the oil phase content of double emulsion can achieve 90% or more, much higher than common High Internal Phase Emulsion, together
When reduce the dosage of surfactant, avoid lamination of the lotion in storage, stability is more preferable.
2, phase gel emulsion has tridimensional network in the DHA algal oil height of the utility model preparation, can obviously improve height
The unstable phenomenons such as bleed, condensate oil in fat liquor storage, DHA algal oil are locked in internal cavities, reduce system oxygen content,
Performance for stability is promoted, also controllable DHA algal oil Targeting delivery and the release for slowing down flavor substance.Green-tea extract is anti-oxidant
Ability can slow down by force DHA algal oil oxidation, and green tea faint scent can good cover algae oil fishy smell.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the preparation facilities of phase double emulsion gel in a kind of DHA algal oil height in the utility model.
Specific embodiment:
In order to which the above objects, features, and advantages of the utility model are more clearly understood, with reference to the accompanying drawing and
The utility model is described in further detail for embodiment.It should be clear that these examples are merely to illustrate the utility model still
It is not limited only to the scope of the utility model.
The utility model discloses a kind of preparation facilities of phase double emulsion gel in DHA algal oil height, including oil mutually to feed
Mouth 1, micro- magnetic ball impact chamber 2, magnetic ball impact chamber 3, discharge port 4 and the first, second water phase injection port 5,6；The oil is mutually fed
Mouthful the 1, first water phase injection port 5 is connected to the side of micro- magnetic ball impact chamber 2 respectively, micro- magnetic ball impact chamber 2 it is another
Side is connected to the magnetic ball impact chamber 3, and the second water phase injection port 6 is connected to the magnetic ball impact chamber 3；Micro- magnetic ball is hit
It hits chamber 2 and magnetic ball impact chamber 3 is all set in alternating magnetic field, if being equipped with inside micro- magnetic ball impact chamber 2 and magnetic ball impact chamber 3
Dry magnetic ball, oily phase feed liquid enter micro- magnetic ball impact chamber 2 by oily phase injection port 1, and aqueous phase liquid is entered micro- by the first water phase feed inlet 5
Magnetic ball impact chamber 2.Under the action of alternating magnetic field, magnetic ball inside micro- magnetic ball impact chamber 2 is high with aqueous phase liquid and oily phase feed liquid
Frequency collides, and achievees the effect that grease merges, obtains lotion；Aqueous phase liquid can be hit by the second water phase feed inlet 6 into magnetic ball later
Chamber 3 is hit, is mixed in 3 inside of magnetic ball impact chamber with the lotion flowed out in micro- magnetic ball impact chamber 2, while in the work for adding alternating magnetic field outside
With lower mutual shock, after oil water mixture double emulsions, is flowed out from discharging pipeline 4, cream is crosslinked by calcium carbonate-gluconolactone
Clear protein isolate is aided with dynamic magnetic ball impact technology to prepare lotion, so that the oil phase content of double emulsion can achieve 90%
More than, much higher than common High Internal Phase Emulsion, while reducing the dosage of surfactant, avoids lotion in storage
Lamination, stability is more preferable.
The diameter of magnetic ball is equal in micro- magnetic ball impact chamber 2；The magnetic ball placed inside the magnetic ball impact chamber 3 is two kinds
Different-diameter can make the more uniform of material impacting, and the oil phase content of oil water mixture double emulsion can be made far high
In common High Internal Phase Emulsion.
Embodiment 1
(1) pre-process: by 5kg gelatin, 0.2kg green-tea extract is dissolved in 100kg water, 500rpm stirring and dissolving, is adjusted
PH to 6 is saved, is obtained as aqueous phase liquid A；By 5kg whey protein isolate, 534g glucolactone and 150g dissolution of calcium carbonate in
In 100kg drinking water, 500rpm is stirred to being completely dissolved, and then heats 30min at 85 DEG C, obtains aqueous phase liquid B；
(2) preparation of substance lotion: oil is obtained after 150kg DHA algal oil and the mixing of 3kg polyglycereol poly ricinoleate
Phase feed liquid is imported under 70MPa high pressure in the oily phase injection port 1 of dynamic magnetic ball impact device, while aqueous phase liquid A is in 70MPa
It is imported under pressure from the first water phase injection port 5；Magnetic ball, water phase material under the action of alternating magnetic field, inside micro- magnetic ball impact chamber 2
Liquid A and the oily mutual high frequency of phase feed liquid are hit, and are achieved the effect that grease merges, are obtained colostric fluid；
(3) preparation of double emulsion: using and import aqueous phase liquid B from the second water phase injection port 6 in 70MPa high pressure, In
Under the action of alternating magnetic field, magnetic ball, aqueous phase liquid B and colostric fluid inside magnetic ball impact chamber 3 are hit mutually, from discharging pipeline 4
Cooling after export, product is detected.
Embodiment 2
(1) pre-process: by 5kg gelatin, 0.2kg green-tea extract is dissolved in 100kg water, 500rpm stirring and dissolving, is adjusted
PH to 6 is saved, is obtained as aqueous phase liquid A；By 5kg whey protein isolate, 534g glucolactone and 150g dissolution of calcium carbonate in
In 100kg drinking water, 500rpm is stirred to being completely dissolved, and then heats 30min at 85 DEG C, obtains aqueous phase liquid B；
(2) preparation of substance lotion: oil is obtained after 150kg DHA algal oil and the mixing of 3kg polyglycereol poly ricinoleate
Phase feed liquid is passed through at dynamic high-pressure Microfluidizer together after mixing aqueous phase liquid A, aqueous phase liquid B and oily phase feed liquid
Reason, processing pressure 70MPa are detected after gained feed liquid is cooling.
Embodiment 3
(1) pre-process: by 5kg gelatin, 0.2kg green-tea extract is dissolved in 100kg water, 500rpm stirring and dissolving, is adjusted
PH to 6 is saved, is obtained as aqueous phase liquid A；5kg whey protein isolate is dissolved in 100kg drinking water, 500rpm is stirred to complete
Dissolution, then heats 30min at 85 DEG C, obtains aqueous phase liquid B；
(2) preparation of substance lotion: after 150kg DHA algal oil and the mixing of 3kg polyglycereol poly ricinoleate, in 60-
It is imported under 80MPa high pressure in the oily phase injection port 1 of dynamic magnetic ball impact device, while 50kg aqueous phase liquid A is pressed in 60-80MPa
It is imported under power from the first water phase injection port 5；Magnetic ball, aqueous phase liquid under the action of alternating magnetic field, inside micro- magnetic ball impact chamber 2
A and the oily mutual high frequency of phase feed liquid are hit, and are achieved the effect that grease merges, are obtained colostric fluid；
(3) preparation of double emulsion: using and import aqueous phase liquid B from the second water phase injection port 6 in 70MPa high pressure, In
Under the action of alternating magnetic field, magnetic ball, aqueous phase liquid B and colostric fluid inside magnetic ball impact chamber 3 are hit mutually, from discharging pipeline 4
Cooling after export, product is detected.
Phase " w/o/w " type double emulsion gel sensory evaluation scores table in table 1 DHA algal oil height
2 Analyses Methods for Sensory Evaluation Results of table
3 physical and chemical property determining result of table
Learnt by the interpretation of result of table 2, table 3 and Fig. 1: the sample of embodiment 1 is a more perfect product.With implementation
Example 1 is compared, and embodiment 2 prepares High Internal Phase Emulsion using traditional dynamic high-pressure Microfluidizer, and product cut size is larger, is easy
There is the flocculation or aggregation of drop, stability, hardness, elastic force is all weaker, and the situation of bleed or condensate oil is more apparent；In embodiment 3
In, product does not use calcium carbonate-gluconolactone crosslinking whey protein isolate to stablize in height to lotion, steady only with emulsifier
Determine lotion, the complete bleed of products obtained therefrom, condensate oil, hardness, elastic force is all poor.Product is common algae oil double emulsion in embodiment 4,
Stability is preferable.The product of embodiment 1 can keep original state after long-term storage, not be in the presence of bleed or condensate oil, and
Emulsion droplet partial size is smaller, is evenly distributed, and has been maximally maintained the original nutritive value of product.The result shows that passing through carbon
Sour calcium-gluconolactone is crosslinked whey protein isolate, is aided with dynamic magnetic ball impact device, can prepare phase " w/o/ in DHA algal oil height
W " type double emulsion gel.
The above description is only the embodiments of the present invention, and therefore it does not limit the scope of the patent of the utility model, needs
Illustrate term " on ", "lower", "left", "right" " top ", " bottom ", "vertical", "horizontal", "inner", "outside" such as occur
Deng, indicated by orientation or positional relationship be based on the orientation or positional relationship shown in the drawings, be merely for convenience of description this
Utility model and simplified description, rather than the device or element of indication or suggestion meaning must have a particular orientation, with specific
Orientation construction and operation, therefore should not be understood as limiting the present invention.In addition, such as there is term " first ", "
Two ", " third " is used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance.In the description of the utility model
In, it should be noted that unless otherwise clearly defined and limited, such as there is term " installation ", " connected ", " connection " should be done extensively
Reason and good sense solution may be a detachable connection for example, it may be being fixedly connected, or the connection of one；It can be mechanical connection,
It can be electrical connection；It can be directly connected, the company inside two elements can also be can be indirectly connected through an intermediary
It is logical.For the ordinary skill in the art, above-mentioned term in the present invention specific can be understood with concrete condition
Meaning, equivalents made by using the description of the utility model and the drawings are applied directly or indirectly in relevant
Technical field is also included in the patent protection scope of the utility model.
Claims (2)
1. the preparation facilities of phase double emulsion gel in a kind of DHA algal oil height, it is characterised in that:
Including oily phase feed inlet (1), micro- magnetic ball impact chamber (2), magnetic ball impact chamber (3), discharge port (4) and the first, second water
Phase injection port (5,6)；
The oil phase feed inlet (1), the first water phase injection port (5) are connected to the side of micro- magnetic ball impact chamber (2) respectively, institute
The other side for stating micro- magnetic ball impact chamber (2) is connected to the magnetic ball impact chamber (3), the second water phase injection port (6) with it is described
Magnetic ball impact chamber (3) connection；
Micro- magnetic ball impact chamber (2) and magnetic ball impact chamber (3) are all set in alternating magnetic field, micro- magnetic ball impact chamber (2)
It is internal equipped with several magnetic balls with magnetic ball impact chamber (3).
2. the preparation facilities of phase double emulsion gel in a kind of DHA algal oil height as described in claim 1, it is characterised in that: institute
The diameter for stating micro- interior magnetic ball of magnetic ball impact chamber (2) is equal；The magnetic ball placed inside the magnetic ball impact chamber (3) is that two kinds of differences are straight
Diameter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822006645.2U CN209549439U (en) | 2018-11-30 | 2018-11-30 | The preparation facilities of phase double emulsion gel in a kind of DHA algal oil is high |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822006645.2U CN209549439U (en) | 2018-11-30 | 2018-11-30 | The preparation facilities of phase double emulsion gel in a kind of DHA algal oil is high |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209549439U true CN209549439U (en) | 2019-10-29 |
Family
ID=68301215
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822006645.2U Active CN209549439U (en) | 2018-11-30 | 2018-11-30 | The preparation facilities of phase double emulsion gel in a kind of DHA algal oil is high |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209549439U (en) |
-
2018
- 2018-11-30 CN CN201822006645.2U patent/CN209549439U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108618146B (en) | Soybean protein-stevioside composite stable phytosterol nano emulsion and preparation method and application thereof | |
| CN104224716B (en) | Utilize the method that nanometer emulsified technology produces nanoparticle | |
| CN209549439U (en) | The preparation facilities of phase double emulsion gel in a kind of DHA algal oil is high | |
| CN109527162A (en) | A kind of walnut protein coffee-whitening powder and preparation method thereof | |
| CN101700225B (en) | Fat emulsion injection and production method thereof | |
| CN103230366B (en) | Novel slow-release breast perfusion agent for preventing cow subclinical mastitis and preparation method thereof | |
| CN109569447A (en) | The preparation facilities and preparation method thereof of phase double emulsion gel in a kind of DHA algal oil is high | |
| CN102657259A (en) | Device and method for producing additive-free yogurt | |
| CN104739724A (en) | Preparation process of natural skincare hydrating micro-emulsified essence composition | |
| CN115281298A (en) | Longjing oat latte beverage and preparation method thereof | |
| CN202680372U (en) | Device for producing yogurt without additives | |
| CN208482313U (en) | One broad sow mixed feed raw material is crushed hybrid system | |
| CN209549438U (en) | A kind of preparation facilities for the snake oil gel containing allantoin | |
| CN105325672A (en) | Edible protein and grease composition and self-assembly method thereof | |
| CN109735392A (en) | A kind of preparation method of high astaxanthin, high phospholipid shrimp sauce | |
| US11964249B2 (en) | Milk protein concentrate-based microencapsulation wall material and microcapsules | |
| CN109433078B (en) | Preparation device and preparation method of high internal phase camellia oil emulsion | |
| CN103393754B (en) | A kind of Cinnamomum longepaniculatum leaf volatile oil emulsion in water | |
| TWI717377B (en) | Micronization device and manufacturing method of product with fluidity using the device | |
| RU2731892C1 (en) | Fodder additive for lactating cows | |
| CN205182533U (en) | High concentration ozone water preparing is equipped with equipment | |
| CN104224715B (en) | A kind of microemulsion containing avilamycin and preparation method thereof | |
| CN213700216U (en) | Buffalo milk fat cracker applying carbon dioxide supercritical fluid | |
| JP2005185181A (en) | Viable cell agent | |
| CN109527161A (en) | A kind of walnut protein instant coffee and preparation method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210309 Address after: 201700 room S214, 2nd floor, building 1, 1288 Huateng Road, Huaxin Town, Qingpu District, Shanghai Patentee after: Kaicheng Health Technology (Shanghai) Co.,Ltd. Address before: No.999, Xuefu Avenue, Honggutan New District, Donghu District, Nanchang City, Jiangxi Province Patentee before: Nanchang University |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220713 Address after: 200000 Room 201, floor 2, building 13, No. 1218, Huateng Road, Huaxin Town, Qingpu District, Shanghai Patentee after: Shanghai Fengsheng Health Technology Co.,Ltd. Address before: 201700 room S214, 2nd floor, building 1, 1288 Huateng Road, Huaxin Town, Qingpu District, Shanghai Patentee before: Kaicheng Health Technology (Shanghai) Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20231122 Address after: 201,700 Room S410, Floor 4, Building 1, No. 1288, Huateng Road, Huaxin Town, Qingpu District, Shanghai Patentee after: Jianqixing Life Sciences (Shanghai) Co.,Ltd. Address before: 200000 Room 201, floor 2, building 13, No. 1218, Huateng Road, Huaxin Town, Qingpu District, Shanghai Patentee before: Shanghai Fengsheng Health Technology Co.,Ltd. |