CN207567146U - A kind of extraction concentrator of vegetable protein - Google Patents
A kind of extraction concentrator of vegetable protein Download PDFInfo
- Publication number
- CN207567146U CN207567146U CN201721196543.0U CN201721196543U CN207567146U CN 207567146 U CN207567146 U CN 207567146U CN 201721196543 U CN201721196543 U CN 201721196543U CN 207567146 U CN207567146 U CN 207567146U
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- reaction kettle
- connecting tube
- enriched chamber
- centrifugal filtration
- vegetable protein
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- 238000000605 extraction Methods 0.000 title claims abstract description 37
- 108010082495 Dietary Plant Proteins Proteins 0.000 title claims abstract description 20
- 238000001914 filtration Methods 0.000 claims abstract description 36
- 238000010438 heat treatment Methods 0.000 claims description 17
- 239000000706 filtrate Substances 0.000 claims description 15
- 238000000227 grinding Methods 0.000 claims description 15
- 239000007788 liquid Substances 0.000 claims description 9
- 230000007246 mechanism Effects 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 8
- 230000000694 effects Effects 0.000 claims description 4
- 238000009413 insulation Methods 0.000 claims description 4
- 238000005119 centrifugation Methods 0.000 claims 1
- 239000003610 charcoal Substances 0.000 claims 1
- 239000005439 thermosphere Substances 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 7
- 238000005516 engineering process Methods 0.000 abstract description 6
- 108090000623 proteins and genes Proteins 0.000 abstract description 4
- 102000004169 proteins and genes Human genes 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 241000196324 Embryophyta Species 0.000 description 17
- 239000000463 material Substances 0.000 description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 12
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 11
- 239000012141 concentrate Substances 0.000 description 7
- 239000002699 waste material Substances 0.000 description 7
- 238000004821 distillation Methods 0.000 description 5
- 239000002245 particle Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 239000003599 detergent Substances 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 230000008719 thickening Effects 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- BGOFCVIGEYGEOF-UJPOAAIJSA-N helicin Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=CC=CC=C1C=O BGOFCVIGEYGEOF-UJPOAAIJSA-N 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 238000000751 protein extraction Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Coloring Foods And Improving Nutritive Qualities (AREA)
Abstract
The utility model belongs to extraction equipment technical field, more particularly to a kind of extraction concentrator of vegetable protein, including reaction kettle, centrifugal filtration room and enriched chamber, the centrifugal filtration room is connected by the first connecting tube with reaction kettle, and the enriched chamber is connected by the second connecting tube with centrifugal filtration room；The utility model is simple in structure, easy to maintain, and production efficiency is greatly improved, and extraction and the concentration technology of vegetable protein can be realized by a procedure, and obtained protein product complies with standard, and concentration purity is high, highly practical, is suitble to promote in this field.
Description
Technical field
The utility model belongs to vegetable protein extractive technique field, and in particular to a kind of extraction concentration of vegetable protein is set
It is standby.
Background technology
It is well known that there is very high nutritive value containing abundant phytoprotein, phytoprotein in plant, so
Phytoprotein is widely used in various food, feed, medicinal material and nutriment etc..
The acquisition methods of phytoprotein be usually first by plant mill into powdered, then by plant powder and water and its
He obtains extracting solution at extractant mixing extraction, finally concentrates extracting solution, wherein, extraction process is with concentration technology for most
The quality of the phytoprotein obtained afterwards has very big relationship, and the extraction of existing phytoprotein extracting solution and concentration technology are mostly
Separated, wherein, extraction process often there are being crushed to plant material when, it is inadequate due to being crushed to plant material
Fully and completely phenomena such as, the concentration technology of phytoprotein extracting solution are exactly often that extracting solution is carried out heating distillation so that carry
The moisture evaporation of liquid is taken, and then obtains concentrate, but in distillation process, is heated in container bottom, so meeting
Lead to extracting solution uneven heating, some extracting solutions too protein structure of Gao Qinei that is heated can be destroyed, and distillation process is big
It all carries out in air, extracting solution easily generates impurity with air reaction in a heated state, these factors can all cause
Obtained phytoprotein concentrate purity is not high, so as to reduce productivity effect, therefore, a kind of good phytoprotein extraction
Liquid concentrator requires study.
Utility model content
In view of the foregoing, the purpose of this utility model is to provide a kind of qualities that can improve phytoprotein extraction
With a kind of extraction concentrator of vegetable protein of efficiency.
Technical solution is used by the utility model：A kind of extraction concentrator of vegetable protein, including reaction kettle, from
Heart filter chamber and enriched chamber, the centrifugal filtration room are connected by the first connecting tube with reaction kettle, and the enriched chamber passes through second
Connecting tube is connected with centrifugal filtration room；The reaction kettle includes feed inlet, and the feed inlet is set to reaction kettle upper end and causes
Reaction kettle outside feed inlet by connecting；The feed inlet lower end connection is through with a grinding device, and the grinding device is by multiple
The mill ball composition being disposed adjacent；The reaction kettle center is equipped with agitating device, and the agitating device extends to reaction kettle ontology
Interior, the agitating device includes being set to the first driving motor of reaction kettle upper end, the agitating shaft connecting with the first driving motor,
And be placed in the poking bar of agitating shaft both ends and bottom, positioned at agitating shaft both sides poking bar by the long poking bar that is staggered and
Short poking bar composition, positioned at the poking bar for stirring shaft end in the shape of a spiral；The inner wall of the enriched chamber is from inside to outside successively
It is divided into heat-conducting layer, heating layer and thermal insulation layer, offers exhaust outlet at the top of the enriched chamber, the interior bottom of the enriched chamber is provided with
Rotating mechanism, the rotating mechanism include being set on the third driving motor of enriched chamber bottom and connect and pass through with third driving motor
Wear the shaft inside enriched chamber, the shaft is equipped with the long paddle being staggered and short paddle, the enriched chamber it is upper
End connects a vacuum extractor by third connecting tube, and the lower end of the enriched chamber is filled by the 4th connecting tube and the collection being equipped with
Put connection.
In addition, the utility model also provides following attached technical scheme：
Preferably, the reaction kettle ontology lower end is connected with funnel type discharge port, and the discharge outlet is equipped with filter layer, institute
Discharge port is stated to connect with centrifugal filtration room by the first connecting tube.
Preferably, the centrifugal filtration chamber interior is equipped with concentrator bowl, and the concentrator bowl lower end is equipped with the second driving motor；Institute
Centrifugal filtration chamber interior bottom end is stated equipped with activated carbon filter layer, centrifugal filtration outdoor lower end is equipped with filtrate (liquid；The filtrate
Exit is connected with the second connecting tube being interconnected with enriched chamber.
Preferably, first connecting tube, the second connecting tube, third connecting tube, the 4th connecting tube and exhaust outlet are divided equally
It She You not valve；Closure valve can according to circumstances be opened.
Preferably, temperature controller is equipped with outside the enriched chamber, the temperature controller is electrically connected with heating layer, institute
Heating layer is stated as the adjustable constant temperature warming layer of temperature；The temperature of convenient accurate control enriched chamber, according to different plant varieties
And different concentration necessary etc., different thickening temperatures is set, improves the quality of vegetable protein extraction.
Preferably, it is equipped with switch controlling device outside the reaction kettle；Avoid waste or production accident.
Preferably, the concentrator bowl side wall position is equipped with the filter opening of connectivity.
In use, plant material is put into receiving hopper, plant material is fully cut and is sent to stirring by cutting chamber
Room, teeter chamber are sufficiently stirred again, crush plant material more complete, the polysaccharide molecule in plant can be more
More flows out with juice, improves the efficiency of extraction；When juice passes through filter screen, can filter out contain in juice it is larger solid
Body waste residue,
Then centrifugal filtration room is entered by first pipe, the concentrator bowl in centrifugal filtration room is by the molecule in juice
Object is filtered, then carries out adsorption filtration to the finely ground particles in juice by activated carbon filter layer so that filtrate and waste residue point
From more completely, last resulting product complies with standard, purity higher.
When the utility model is used, plant material is put into feed inlet, plant material is fully ground by grinding device,
Reaction extraction in reaction kettle is then fed into, at this point, the first driving motor drives poking bar in reaction kettle by the raw material after grinding
It is sufficiently stirred, improves the efficiency of extraction；Then connect in reaction kettle tail portion with centrifugal filtration room by setting funnel
Type discharge port improves the efficiency of discharging, and is setting filter layer in discharge port, can filter out the larger solid contained in juice
Waste residue then enters centrifugal filtration room by the first connecting tube, and the concentrator bowl in centrifugal filtration room is by the molecule in juice
Object is filtered, then carries out adsorption filtration to the finely ground particles in juice by activated carbon filter layer so that filtrate and waste residue point
From more completely, since obtained filter liquor concentration is not met by the concentration mark of detergent after being filtered by centrifugal filtration room
Standard, therefore obtained filtrate is entered enriched chamber by the utility model by the second connecting tube, into after enriched chamber, startup vacuumizes
Air inside device enriched chamber is taken away, is allowed to become vacuum state, is then shut off the vacuum extractor, then starting switch
So that the heating layer is begun to warm up, the heat that heating layer generates can be eventually transferred to filtrate through the heat-conducting layer, this stage can
Adjustment temperature as needed, while start the rotating mechanism and start that the paddle is driven to be stirred work so that it is entire
Being heated evenly for extracting solution, further speeds up distillation speed, is then turned on exhaust outlet discharge evaporative air, and liquid to be extracted is concentrated to
During the degree needed, the switch of all devices is shut off, obtains concentrate, when solution to be concentrated is cooled to room temperature, valve is opened,
Concentrate is made to enter collection device, you can complete entire extraction concentration process.
In conclusion the utility model has following advantageous effect：
1st, after the grinding that the utility model passes through grinding device, by stirring, make plant material crush it is more thorough, and
Poking bar for stirring is that the poking bar to be interlocked by length is combined into so that material is uniformly mixed, and agitating device bottom is also
Equipped with spiral helicine poking bar, the material of reaction kettle body bottom portion is stirred again, be allowed to mixing it is more abundant, by grinding
And the plant material granularity after stirring becomes very little, extraction efficiency is high in a kettle, alleviates phytoprotein extraction
Working procedure shortens extraction time, improves the efficiency of phytoprotein extraction.
What the 2nd, the utility model filtrate detached with waste residue is more complete, and obtained filtrate purity higher improves vegetable protein
The quality of extraction.
3rd, the utility model enriched chamber is simple in structure, and principle is understandable, obtained extracting solution can be concentrated, setting
Heating layer accelerates distilling rate, and setting paddle makes material integrally be heated evenly, substantially increases thickening efficiency, and concentration process
The destruction that protein structure is subject to is smaller.
In conclusion the utility model is simple in structure, and it is easy to maintain, production efficiency is greatly improved, passes through one of work
Extraction and the concentration technology of vegetable protein can be realized in sequence, and obtained protein product complies with standard, and concentration purity is high, practical
Property it is strong, be suitble to this field promote.
Description of the drawings
Fig. 1 is the structure diagram of the utility model；
Parts title and serial number in figure：
Reaction kettle 1, feed inlet 11, grinding device 12, the first driving motor 13, agitating shaft 14, short poking bar 15, long stirring
Rod 16, poking bar 17, switch controlling device 18, discharge port 19, centrifugal filtration room 2, concentrator bowl 21, activated carbon filter layer 22, the
Two driving motors 23, enriched chamber 3, vacuum extractor 31, collection device 32, rotating mechanism 33, third driving motor 331, shaft
332, long paddle 333, short paddle 334, thermal insulation layer 34, heating layer 35, heat-conducting layer 36, temperature controller 37, exhaust outlet 38,
First connecting tube 4, the second connecting tube 5, third connecting tube 6, the 4th connecting tube 7, valve 8.
Specific embodiment
Technical solutions of the utility model are made below in conjunction with preferred embodiment and its attached drawing further unrestricted detailed
Explanation.
Embodiment 1：
As shown in Figure 1, a kind of extraction concentrator of vegetable protein, including reaction kettle 1, centrifugal filtration room 2 and enriched chamber
3, centrifugal filtration room 2 is connected by the first connecting tube 4 with reaction kettle 1, and enriched chamber 3 passes through the second connecting tube 5 and centrifugal filtration room 2
Connection；1 outside of reaction kettle is equipped with switch controlling device 18.
Wherein, reaction kettle 1 include feed inlet 11, feed inlet 11 be set to 1 upper end of reaction kettle and cause reaction kettle 1 by into
It is connected outside material mouth 11；1 ontology lower end of reaction kettle is connected with funnel type discharge port 19, and filter layer, institute are equipped at the discharge port 19
Discharge port 19 is stated to connect with centrifugal filtration room 2 by the first connecting tube 4；The connection of 11 lower end of feed inlet is through with a grinding device
12, grinding device 12 is made of multiple mill balls being disposed adjacent, and the setting of the grinding device 12 can will need the plant extracted
Object is ground into powder, and improves the efficiency of later stage extraction；1 center of reaction kettle is equipped with agitating device, and agitating device extends to reaction
In 1 ontology of kettle, agitating device includes being set to the first driving motor 13 of 1 upper end of reaction kettle, be connect with the first driving motor 13
Agitating shaft 14 and be placed in the poking bar 17 of 14 both ends of agitating shaft and bottom, positioned at 14 both sides of agitating shaft poking bar 17 by
The long poking bar 333 that is staggered and short stirring 334 rods composition, positioned at 14 end of agitating shaft poking bar 17 in the shape of a spiral.
Centrifugal filtration room 2 is internally provided with concentrator bowl 21, and 21 lower end of concentrator bowl is equipped with the second driving motor 23；Centrifugal filtration room
2 inner bottoms are equipped with activated carbon filter layer 22, and 2 outside lower end of centrifugal filtration room is equipped with filtrate (liquid；It is connected at filtrate (liquid
The second connecting tube 5 being interconnected with enriched chamber 3；21 side wall position of concentrator bowl is equipped with the filter opening of connectivity.
The inner wall of enriched chamber 3 is divided into heat-conducting layer 36, heating layer 35 and thermal insulation layer 34,3 top of enriched chamber from inside to outside
Exhaust outlet 38 is offered, the interior bottom of enriched chamber 3 is provided with rotating mechanism 33, and rotating mechanism 33 includes being set on 3 bottom of enriched chamber
Third driving motor 331 and connect with third driving motor 331 and the shaft 332 inside the enriched chamber 3, in shaft 332
Equipped with the long paddle 333 and short paddle 334 being staggered, the upper end of enriched chamber 3 is taken out very by the connection of third connecting tube 6 one
Empty device 31, the lower end of enriched chamber 3 are connected by the 4th connecting tube 7 with collection device 32；3 outside of enriched chamber is equipped with temperature and controls
Device 37, temperature controller 37 are electrically connected with heating layer 35, and heating layer 35 is the adjustable constant temperature warming layer 35 of temperature.
Above-mentioned the first connecting tube 4, the second connecting tube 5, third connecting tube 6, the 4th connecting tube 7 and exhaust outlet 38 is divided equally
It She You not valve 8, convenient opening as needed or closing valve 8.
The course of work for a kind of extraction concentrator of vegetable protein of the utility model below：In use, by plant original
Material is put into feed inlet 11, and plant material is fully ground by grinding device 12, is then fed into reaction extraction in reaction kettle 1, at this point,
First driving motor 13 drives the poking bar 17 in reaction kettle 1 to be sufficiently stirred the raw material after grinding, improves extraction
Efficiency；Then connect in 1 tail portion of reaction kettle with centrifugal filtration room 2 by setting funnel type discharge port 19, improve the effect of discharging
Rate, and filter layer is being set in discharge port 19, the larger solid slag contained in juice can be filtered out, then passes through first
Connecting tube 4 enters centrifugal filtration room 2, and the finely ground particles in juice are filtered by the concentrator bowl 21 in centrifugal filtration room 2, then
Adsorption filtration is carried out to the finely ground particles in juice by activated carbon filter layer 22 so that filtrate detached with waste residue more adds
Entirely, since the filter liquor concentration obtained after being filtered by centrifugal filtration room 2 is not met by the concentration standard of detergent, this reality
Obtained filtrate is entered into enriched chamber 3 by the second connecting tube 5 with novel, into after enriched chamber 3, it is dense to start vacuum extractor 31
The air of contracting chamber interior is taken away, is allowed to become vacuum state, is then shut off the vacuum extractor 31, and then starting switch causes
The heating layer 35 is begun to warm up, and the heat that heating layer generates can be eventually transferred to filtrate through the heat-conducting layer 36, this stage can
Adjustment temperature as needed, while start the rotating mechanism 33 and start that the paddle is driven to be stirred work so that it is whole
Being heated evenly for a extracting solution, further speeds up distillation speed, is then turned on exhaust outlet 38 and discharges evaporative air, liquid to be extracted is dense
When being reduced to the degree of needs, the switch of all devices is shut off, obtains concentrate, when solution to be concentrated is cooled to room temperature, by valve
It opens, concentrate is made to enter collection device 32, you can complete entire extraction concentration process.
It should be pointed out that above description is the detailed description for the preferable possible embodiments of the utility model, but implement
Example is not limited to the patent claim of the utility model, is completed under the technical spirit suggested by all the utility model
Equal variation or modification change, should all belong to the utility model and cover the scope of the claims.
Claims (7)
1. the extraction concentrator of a kind of vegetable protein, which is characterized in that including reaction kettle, centrifugal filtration room and enriched chamber, institute
It states centrifugal filtration room to connect with reaction kettle by the first connecting tube, the enriched chamber is connected by the second connecting tube and centrifugal filtration room
It is logical；The reaction kettle includes feed inlet, and the feed inlet is set to reaction kettle upper end and so that reaction kettle is connected outside by feed inlet
It is logical；The feed inlet lower end connection is through with a grinding device, and the grinding device is made of multiple mill balls being disposed adjacent；
The reaction kettle center is equipped with agitating device, and the agitating device is extended in reaction kettle ontology, and the agitating device includes setting
The first driving motor for being placed in reaction kettle upper end, the agitating shaft being connect with the first driving motor and be placed in agitating shaft both ends and
The poking bar of bottom, the poking bar positioned at agitating shaft both sides is made of the long poking bar being staggered and short poking bar, positioned at institute
State the poking bar of stirring shaft end in the shape of a spiral；The inner wall of the enriched chamber be divided into from inside to outside heat-conducting layer, heating layer and
Thermal insulation layer, the enriched chamber top offer exhaust outlet, and the interior bottom of the enriched chamber is provided with rotating mechanism, the whirler
Structure includes being set on the third driving motor of enriched chamber bottom and is connect with third driving motor and run through the shaft inside enriched chamber,
The shaft is equipped with the long paddle being staggered and short paddle, the upper end of the enriched chamber are connected by third connecting tube
One vacuum extractor, the lower end of the enriched chamber are connected by the 4th connecting tube with the collection device being equipped with.
A kind of 2. extraction concentrator of vegetable protein according to claim 1, which is characterized in that the reaction kettle ontology
Lower end is connected with funnel type discharge port, and the discharge outlet is equipped with filter layer, and the discharge port passes through the first connecting tube and centrifugation
Filter chamber connects.
A kind of 3. extraction concentrator of vegetable protein according to claim 1, which is characterized in that the centrifugal filtration room
Concentrator bowl is internally provided with, the concentrator bowl lower end is equipped with the second driving motor；The centrifugal filtration chamber interior bottom end is equipped with activity
Charcoal filter layer, centrifugal filtration outdoor lower end are equipped with filtrate (liquid；It is connected at the filtrate (liquid and is interconnected with enriched chamber
The second connecting tube.
A kind of 4. extraction concentrator of vegetable protein according to claim 1, which is characterized in that first connection
Pipe, the second connecting tube, third connecting tube, the 4th connecting tube and exhaust outlet are respectively equipped with valve.
5. the extraction concentrator of a kind of vegetable protein according to claim 1, which is characterized in that outside the enriched chamber
Equipped with temperature controller, the temperature controller is electrically connected with heating layer, and the heating layer is the adjustable constant temperature hair of temperature
Thermosphere.
6. the extraction concentrator of a kind of vegetable protein according to claim 1, which is characterized in that outside the reaction kettle
Equipped with switch controlling device.
A kind of 7. extraction concentrator of vegetable protein according to claim 2, which is characterized in that the concentrator bowl side wall
Position is equipped with the filter opening of connectivity.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721196543.0U CN207567146U (en) | 2017-09-18 | 2017-09-18 | A kind of extraction concentrator of vegetable protein |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721196543.0U CN207567146U (en) | 2017-09-18 | 2017-09-18 | A kind of extraction concentrator of vegetable protein |
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| Publication Number | Publication Date |
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| CN207567146U true CN207567146U (en) | 2018-07-03 |
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ID=62697374
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| CN201721196543.0U Active CN207567146U (en) | 2017-09-18 | 2017-09-18 | A kind of extraction concentrator of vegetable protein |
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| CN108728583A (en) * | 2018-08-13 | 2018-11-02 | 安吉艾格赛思生物科技有限公司 | A kind of concentrating and purifying device of xylo-oligosaccharide |
| CN108728582A (en) * | 2018-08-13 | 2018-11-02 | 安吉艾格赛思生物科技有限公司 | A kind of equipment efficiently preparing functional low polyxylose |
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| CN109692642A (en) * | 2019-01-16 | 2019-04-30 | 江苏新鑫隆医药科技股份有限公司 | Two-in-one filter device |
| CN109954293A (en) * | 2018-12-03 | 2019-07-02 | 湖南全望信息科技有限公司 | A kind of industrial design solid material dissolution extraction element |
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| CN111921225A (en) * | 2020-08-21 | 2020-11-13 | 任平红 | Tea polyphenol extraction system and extraction process |
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| CN108728583B (en) * | 2018-08-13 | 2024-04-12 | 青岛瑞利恩生物科技有限公司 | Concentration purification device of xylooligosaccharide |
| CN108728583A (en) * | 2018-08-13 | 2018-11-02 | 安吉艾格赛思生物科技有限公司 | A kind of concentrating and purifying device of xylo-oligosaccharide |
| CN109277038A (en) * | 2018-11-20 | 2019-01-29 | 广东石油化工学院 | An integrated device for mixing and filtering wine and water for wine making |
| CN109954293A (en) * | 2018-12-03 | 2019-07-02 | 湖南全望信息科技有限公司 | A kind of industrial design solid material dissolution extraction element |
| CN109692642A (en) * | 2019-01-16 | 2019-04-30 | 江苏新鑫隆医药科技股份有限公司 | Two-in-one filter device |
| CN111116739A (en) * | 2020-01-23 | 2020-05-08 | 中科宝承生物医学科技有限公司 | Antibody concentration equipment and operation method thereof |
| CN111378005B (en) * | 2020-04-03 | 2021-08-17 | 安徽环球基因科技有限公司 | Adjustable protein purifying device |
| CN111378005A (en) * | 2020-04-03 | 2020-07-07 | 安徽环球基因科技有限公司 | Adjustable protein purifying device |
| CN111482284B (en) * | 2020-04-09 | 2021-09-24 | 上海理真堂实业有限公司 | Traditional chinese medicine draws uses centrifuge |
| CN111482284A (en) * | 2020-04-09 | 2020-08-04 | 李环 | Traditional chinese medicine draws uses centrifuge |
| CN111921225A (en) * | 2020-08-21 | 2020-11-13 | 任平红 | Tea polyphenol extraction system and extraction process |
| CN112933653A (en) * | 2021-02-02 | 2021-06-11 | 郑州市鑫磊香料有限公司 | Tamarind fruit extract purification equipment and technology |
| CN113019288A (en) * | 2021-03-09 | 2021-06-25 | 威海市和谐硅业有限公司 | Device and method for optimizing production of silane coupling agent |
| CN113019288B (en) * | 2021-03-09 | 2022-05-20 | 威海市和谐硅业有限公司 | Device and method for optimizing production of silane coupling agent |
| CN113828053A (en) * | 2021-10-21 | 2021-12-24 | 丽江英煌集生物工程有限公司 | Separation and purification preparation device and separation and purification method for maca polysaccharide |
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| CN115414697A (en) * | 2022-08-31 | 2022-12-02 | 河南联源生物科技股份有限公司 | Extraction equipment and extraction method for extracting active dendrobium polysaccharide from dendrobium |
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