CN206103401U - Vegetable protein draws concentrator - Google Patents
Vegetable protein draws concentrator Download PDFInfo
- 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
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- delivery outlet
- input port
- stoste
- concentrate
- vegetable protein
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- 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
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.
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)
| 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 |
-
2016
- 2016-09-30 CN CN201621099881.8U patent/CN206103401U/en active Active
Cited By (2)
| 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 |
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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. |