CN207567146U - A kind of extraction concentrator of vegetable protein - Google Patents

A kind of extraction concentrator of vegetable protein Download PDF

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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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陈玫辛
田新风
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陈玫辛
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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

A kind of extraction concentrator of vegetable protein
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.
CN201721196543.0U 2017-09-18 2017-09-18 A kind of extraction concentrator of vegetable protein Active CN207567146U (en)

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Application Number Priority Date Filing Date Title
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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
CN111378005A (en) * 2020-04-03 2020-07-07 安徽环球基因科技有限公司 Adjustable protein purifying device
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
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

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
CN111378005A (en) * 2020-04-03 2020-07-07 安徽环球基因科技有限公司 Adjustable protein purifying device
CN111378005B (en) * 2020-04-03 2021-08-17 安徽环球基因科技有限公司 Adjustable protein purifying device
CN111482284A (en) * 2020-04-09 2020-08-04 李环 Traditional chinese medicine draws uses centrifuge
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
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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