CN206103401U - Vegetable protein draws concentrator - Google Patents

Vegetable protein draws concentrator Download PDF

Info

Publication number
CN206103401U
CN206103401U CN201621099881.8U CN201621099881U CN206103401U CN 206103401 U CN206103401 U CN 206103401U CN 201621099881 U CN201621099881 U CN 201621099881U CN 206103401 U CN206103401 U CN 206103401U
Authority
CN
China
Prior art keywords
delivery outlet
input port
stoste
concentrate
vegetable protein
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
Application number
CN201621099881.8U
Other languages
Chinese (zh)
Inventor
熊鸣
熊一鸣
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guangdong Jiaxia Daily Necessities Technology Co ltd
Original Assignee
Guangzhou City Jiaqian Ya Cosmetics Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Guangzhou City Jiaqian Ya Cosmetics Co Ltd filed Critical Guangzhou City Jiaqian Ya Cosmetics Co Ltd
Priority to CN201621099881.8U priority Critical patent/CN206103401U/en
Application granted granted Critical
Publication of CN206103401U publication Critical patent/CN206103401U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Peptides Or Proteins (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

Vegetable protein draws concentrator is including the concentrated jar of reation kettle, solid residue filters jar, albumen liquid holding vessel, albumen liquid of order connection, the reation kettle top is equipped with the raw material input mouth, and the bottom is equipped with the stoste delivery outlet, solid residue filters tank deck portion is equipped with the stoste input port of connecting the stoste delivery outlet, and the bottom is equipped with residue discharge port and filtrating delivery outlet, albumen liquid holding vessel top is equipped with the filtrating input port of connecting the filtrating delivery outlet, and the bottom is equipped with concentrate delivery outlet and circulation delivery outlet, the concentrated tank deck portion of albumen liquid is equipped with the circulation input port of connecting the circulation delivery outlet, and the bottom is equipped with waste water delivery outlet and concentrate and retrieves mouthful, the concentrate retrieve mouthful also with albumen liquid holding vessel on filtrating input port connection. The utility model discloses simple structure, easy to maintain, it is high to have increased substantially production efficiency, through one process can realize vegetable protein draw with concentrated technology, optimized the molecular weight of vegetable protein extract product through the loop filter concentration, more easily store and use.

Description

Vegetable protein extracts concentrator
Technical field
The utility model is related to vegetable protein extractive technique field, and specifically vegetable protein extracts concentrator.
Background technology
At present, ecosystem, the environmental protection index of product are increasingly paid attention in daily use chemicals cleaning supplies, more day is derived from using addition The active ingredient of right plant, such as vegetable protein is exactly one of adding ingredient for cleaning agent production.
All extracted using reactor extraction by vegetable protein, the protein concentration in extract is not enough to directly should For the production of cleaning agent, further concentration purification is needed.The technique and equipment of protein liquid concentration purification is even more important, improperly Technical scheme will cause the waste of a large amount of protein resources, and also serious environment pollution, can also increase energy resource consumption and life Produce cost.
Utility model content
The utility model is in order to overcome above-mentioned prior art weak point, there is provided a kind of vegetable protein extracts concentration and sets It is standby.
Specifically, the utility model employs following technical scheme.
Vegetable protein extracts concentrator, including reactor, solid residue filtering tank, the protein liquid storage being linked in sequence Tank, protein liquid concentration tank;Reactor top is provided with feedstock input, and bottom is provided with stoste delivery outlet;Solid residue filters tank deck Portion is provided with the stoste input port of connection stoste delivery outlet, and bottom is provided with residue floss hole and filtrate outlet;Protein liquid holding vessel Top is provided with the filtrate input port of connection filtrate outlet, and bottom is provided with concentrate delivery outlet and circulation delivery outlet;Protein liquid is dense Contracting tank top is provided with the circulation input port of connection circulation delivery outlet, and bottom is provided with waste water delivery outlet and concentrate recovery port, concentrates Liquid recovery port is also connected with the filtrate input port on protein liquid holding vessel.
Compared with prior art, the beneficial effects of the utility model are:It is simple structure, easy to maintain, increase substantially Production efficiency is high, and by a procedure extraction and the concentration technology of vegetable protein can be realized, is concentrated by circulating filtration excellent The molecular weight of vegetable protein extract is changed, process products are more easily stored and used.
Description of the drawings
Fig. 1 is structural representation of the present utility model.
Specific embodiment
As shown in figure 1, vegetable protein extract concentrator, including the reactor 1, solid residue filtering tank 2 being linked in sequence, Protein liquid holding vessel 3, protein liquid concentration tank 4;The top of reactor 1 is provided with feedstock input 11, and bottom is provided with stoste delivery outlet 12; The top of solid residue filtering tank 2 is provided with the stoste input port 21 of connection stoste delivery outlet 12, and bottom is provided with the He of residue floss hole 22 Filtrate outlet 23;The top of protein liquid holding vessel 3 is provided with the filtrate input port 31 of connection filtrate outlet 23, and bottom is provided with concentration Liquid delivery outlet 32 and circulation delivery outlet 33;The top of protein liquid concentration tank 4 is provided with the circulation input port 41 of connection circulation delivery outlet 33, Bottom is provided with waste water delivery outlet 43 and concentrate recovery port 42, concentrate recovery port 42 also with protein liquid holding vessel 3 on filtrate Input port 31 connects.
Its operation principle is as follows:
(1) raw material is put into reactor 1 by feedstock input 11, carries out vegetable protein extraction, after albumen stoste is obtained, Passed through stoste delivery outlet 12, stoste input port 21 and be transported to solid residue filtering tank 2;
(2) it is after solid residue filtering tank 2 filters solid residue, filtrate is defeated through filtrate outlet 23, filtrate Entrance 31 is transported to protein liquid holding vessel 3, and solid residue is then excluded from residue floss hole 22;
(3) filtrate in protein liquid holding vessel 3 is transported to protein liquid concentration through circulation delivery outlet 33, circulation input port 41 Filtrate is filtered into concentrate egg white liquor by tank 4, protein liquid concentration tank 4, and by concentrate recovery port 42, filtrate input port 31 will be dense Pix protein liquid send back to protein liquid holding vessel 3 deposit or again circulating filtration until concentrate egg white liquor meets technological standards;
(4) technological standards concentrate egg white liquor will be met and exports standby from the concentrate delivery outlet 32 of protein liquid holding vessel 3.
Preferably, protein liquid concentration tank 4 employs ultrafiltration membrance filter structure.
For a person skilled in the art, it is each that structure and principle that can be according to disclosed in the utility model obtain other It is kind corresponding to change and deform, and all these changes and deformation belongs to protection category of the present utility model.

Claims (2)

1. vegetable protein extracts concentrator, it is characterised in that:Including the reactor, solid residue filtering tank, the egg that are linked in sequence White liquor holding vessel, protein liquid concentration tank;Reactor top is provided with feedstock input, and bottom is provided with stoste delivery outlet;Solid residue Filtering tank top is provided with the stoste input port of connection stoste delivery outlet, and bottom is provided with residue floss hole and filtrate outlet;Albumen Liquid concentration tank top is provided with the filtrate input port of connection filtrate outlet, and bottom is provided with concentrate delivery outlet and circulation delivery outlet; Protein liquid concentration tank top is provided with the circulation input port of connection circulation delivery outlet, and bottom is provided with waste water delivery outlet and concentrate is reclaimed Mouthful, concentrate recovery port is also connected with the filtrate input port on protein liquid concentration tank.
2. vegetable protein according to claim 1 extracts concentrator, it is characterised in that:Protein liquid concentration tank 4 is employed Ultrafiltration membrance filter structure.
CN201621099881.8U 2016-09-30 2016-09-30 Vegetable protein draws concentrator Active CN206103401U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621099881.8U CN206103401U (en) 2016-09-30 2016-09-30 Vegetable protein draws concentrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621099881.8U CN206103401U (en) 2016-09-30 2016-09-30 Vegetable protein draws concentrator

Publications (1)

Publication Number Publication Date
CN206103401U true CN206103401U (en) 2017-04-19

Family

ID=58522625

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621099881.8U Active CN206103401U (en) 2016-09-30 2016-09-30 Vegetable protein draws concentrator

Country Status (1)

Country Link
CN (1) CN206103401U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111153786A (en) * 2019-12-31 2020-05-15 江苏久吾高科技股份有限公司 Coenzyme Q10 extraction method and device
CN114618186A (en) * 2022-03-19 2022-06-14 莆田市农汇食品有限公司 Natural food aromatic extraction device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111153786A (en) * 2019-12-31 2020-05-15 江苏久吾高科技股份有限公司 Coenzyme Q10 extraction method and device
CN114618186A (en) * 2022-03-19 2022-06-14 莆田市农汇食品有限公司 Natural food aromatic extraction device

Similar Documents

Publication Publication Date Title
CN206103401U (en) Vegetable protein draws concentrator
CN205684416U (en) A kind of Chinese medicine circulation cleaning washing trough
CN101555359A (en) Grape skin red pigment preparation method
CN107585913A (en) Biogas slurry concentrates resource utilization device
CN107555673A (en) A kind of method of high efficiente callback electroforming waste liquid and useless underwater gold
CN203852864U (en) Heat reflux extracting concentrating equipment
CN205794722U (en) A kind of effective content of tea coarse filtration refines system
CN104803516A (en) Integrated container type sea water desalting equipment and desalting process thereof
CN203353611U (en) Soy sauce filtering system
CN205011563U (en) Gelatin production sewage treatment plant
CN206934796U (en) A kind of normal temperature concentrator of rose extract
CN206156876U (en) Useless lye recovery system of chitin production
CN101669551A (en) Production method of low-sugar soya-bean milk
CN103045474A (en) Recovery equipment and technology for hydroxy phenylglycine in amoxicillin synthetic mother solution
CN205556784U (en) Printed circuit board is sour, alkaline copper chloride etching waste liquor cyclic utilization device
CN207628040U (en) A kind of mechanical device quickly removing algae
CN105483706B (en) A kind of printed circuit board acid, alkaline copper chloride etching waste liquid recycling device and its method
CN217808969U (en) Potato starch processing sewage treatment system
CN206081794U (en) Filtrate collecting device
CN205746914U (en) A kind of boiler slag processing means
CN205145993U (en) A equipment for traditional chinese medicine purification
CN205616987U (en) Concentrated system that deposits is recycled to plating solution
CN217600513U (en) Glass deep-processing sewage full-circulation purification system
CN216584307U (en) Contain concentrated recovery system of salt waste water
CN204999746U (en) Be applied to cell membrane layer of domestic drinking water and filter water purifying equipment

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: 20230509

Address after: Room 17, Room 401, 4th Floor, Building A, Enterprise Service Center, No. 1 Guangzhou Road, Guangzhou (Qingyuan) Industrial Transfer Industrial Park, Shijiao Town, Qingcheng District, Qingyuan City, Guangdong Province, 511500

Patentee after: Guangdong Jiaxia Daily Necessities Technology Co.,Ltd.

Address before: No. 128, Zhenhua North Road, Shenshan Industrial Park, Jianggao Town, Baiyun District, Guangzhou, Guangdong 510000

Patentee before: GUANGZHOU CITY GARCIA COSMETICS CO.,LTD.