CN203429169U - Automatic collagen production line - Google Patents
Automatic collagen production line Download PDFInfo
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- CN203429169U CN203429169U CN201320556606.4U CN201320556606U CN203429169U CN 203429169 U CN203429169 U CN 203429169U CN 201320556606 U CN201320556606 U CN 201320556606U CN 203429169 U CN203429169 U CN 203429169U
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- pressure filter
- concentration evaporator
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Abstract
The utility model discloses an automatic collagen production line. The production line comprises a washing pool, a cooking sterilization tank, an enzymatic hydrolysis tank, a filter press, an ion exchanger, a concentration evaporator and a centrifugal spray drier, wherein the washing pool and the cooking sterilization tank are connected through a conveying belt; a baffle is arranged between the washing pool and the cooking sterilization tank; a feed port and a discharge port are formed in the enzymatic hydrolysis tank, the feed port is connected with the cooking sterilization tank through a pump body, and the discharge port is connected with the filter press through the pump body; the filter press is connected with the ion exchanger through the pump; the ion exchanger is connected with the concentration evaporator through the pump; the concentration evaporator is connected with the high-speed centrifugal spray drier through a slurry pump. The automatic collagen production line is simple in structure, easy to control and small in equipment investment, and does not cause environmental pollution; a product is strong in bioactivity, and can be used for preparing health-care food or medicines for resisting oxidation, reducing blood pressure, resisting atherosclerosis or beautifying.
Description
Technical field
The utility model relates to a kind of automatic production line of preparing collagen protein, belongs to biological technical field.
Background technology
Collagen protein (Collagen) collagen protein is comprised of micromolecular polypeptide; by liquid-phase chromatographic analysis, show; the molecular weight of collagen protein is between 500-13000 dalton; its molecular-weight average is in 3000 dalton left and right; that people's in-vivo content is maximum, the widest a kind of protein distributes; account for the 25%-30% of human body internal protein longeron; it is mainly present in skin, kidney, tooth, tendon, ligament and the blood vessel of human body; be the extremely important structural protein of reticular tissue, play the function that supports organ, protection human body.Collagen protein be rich in human body necessary 18 in amino acid, oxyproline wherein and hydroxylysine are the amino acid of holding in collagen protein.Collagen protein is widely used in the functional products such as biomedical material, healthcare products, food, makeup with its good biocompatibility, original specific triple helix structure etc.The preparation of collagen protein is by proteolytic enzyme, pigskin, fish-skin, fish scale, ox-hide and bone etc. to be contained the enzymic hydrolysate of collagen product, by the directed shearing technique extraction process of biological enzyme, when having kept Isin glue collagen activity, by collagen protein enzymolysis to the molecular level of applicable absorption of human body.Still do not prepare at present the automatic production line of collagen protein, more with small workshop mode, as everyone knows, at the best bet aseptic, that be prepared into the collagen protein that meets food sanitation standard that guarantees production process, be exactly to cut down the number of intermediate links as far as possible, automatic production line is safer.
Summary of the invention
Technical problem to be solved in the utility model is intended to provide a kind of automatic production line of preparing collagen protein, is prepared into the collagen product that meets food sanitation standard and have nourishing function.
For solving this technical problem, the utility model provides a kind of collagen protein automatic production line, comprise service sink, boiling sterilization tank, enzyme digestion reaction tank, pressure filter, ion-exchanger, concentration evaporator and centrifugal spray drier, service sink is connected by travelling belt with boiling sterilization tank, between service sink and boiling sterilization tank, be provided with division board, described enzyme digestion reaction tank is provided with opening for feed and discharge port, opening for feed is connected with boiling sterilization tank by the pump housing, discharge port connects pressure filter by the pump housing, pressure filter is connected with ion-exchanger by pump, ion-exchanger is connected with concentration evaporator by pump, described concentration evaporator is connected with hig h-speed centrifugal spray drying device by slush pump.
Described enzyme digestion reaction tank comprises tank body, heating unit, whipping appts, opening for feed and discharge port, and described heating unit is positioned at tank base.
Described pressure filter is hydraulic diaphragm pressure filter.
Described ion-exchanger is provided with three tank bodies, by pipeline, connects successively.
Described concentration evaporator is single-action falling film type thickener.
Described boiling sterilization tank, enzyme digestion reaction tank, pressure filter, ion-exchanger and concentration evaporator are equipped with automatic flushing device.
Beneficial effect: the utility model, by enzymolysis, two-stage filtration and concentrated dusting, is prepared into the collagen product that meets food sanitation standard and have nourishing function, and this automatic production line is simple in structure, is easy to control, and facility investment is few, non-environmental-pollution; In addition, the abundant raw material that the utility model adopts is easy to get, in prepared collagen product, protein content is high, and product has very strong biological activity, can be used for preparing protective foods or the medicine of anti-oxidant, hypotensive, atherosclerosis or beauty treatment.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure: 1 service sink, 2 boiling sterilization tanks, 3 enzyme digestion reaction tanks, 4 pressure filter, 5 ion-exchangers, 6 concentration evaporators, 7 hig h-speed centrifugal spray drying devices, 8 travelling belts, 9 division boards.
Embodiment
Below in conjunction with drawings and Examples, the utility model is specifically described.
Figure 1 shows that structural representation of the present utility model.
The utility model comprises service sink 1, boiling sterilization tank 2, enzyme digestion reaction tank 3, pressure filter 4, ion-exchanger 5, concentration evaporator 6 and centrifugal spray drier 7.
Described service sink 1 is connected by travelling belt 8 with boiling sterilization tank 2, between service sink 1 and boiling sterilization tank 2, be provided with division board 9, described enzyme digestion reaction tank 3 is provided with opening for feed and discharge port, opening for feed is connected with boiling sterilization tank 2 by the pump housing, discharge port connects pressure filter 4 by the pump housing, pressure filter 4 is connected with ion-exchanger 5 by pump, and ion-exchanger 5 is connected with concentration evaporator 6 by pump, and described concentration evaporator 6 is connected with hig h-speed centrifugal spray drying device 7 by slush pump.
Described enzyme digestion reaction tank 3 comprises tank body, heating unit, whipping appts, opening for feed and discharge port, and described heating unit is positioned at tank base.
Described pressure filter 4 is hydraulic diaphragm pressure filter 4.
Described ion-exchanger 5 is provided with three tank bodies, by pipeline, connects successively.
Described concentration evaporator 6 is single-action falling film type thickener.
Described boiling sterilization tank 2, enzyme digestion reaction tank 3, pressure filter 4, ion-exchanger 5 and concentration evaporator 6 are equipped with automatic flushing device.
Technical process of the present utility model is:
Clean (outside)---boiling, high-temperature sterilization (90 ℃)---enzymolysis (60 ℃+gac)---press filtration---centrifugal removal of impurities (ion-exchanger)---concentrated (vaporizer)---spraying (hig h-speed centrifugal spray drying device).
Concrete technology principle is:
In service sink, raw material thawed and cleaned through flowing water, in clean water basin, being provided with die, for bulk raw, carrying out chopped; Raw material after chopped enters boiling sterilization tank by conveying belt, adds 0.2%NaOH solution in boiling sterilization tank, stirs, is heated to 90 ℃, soaks 40 minutes, washes with water to neutrality; Enter in enzyme digestion reaction tank, under stirring, be steam heated to 50 ~ 60 ℃, add Sumizyme MP, the lower stirring reaction of insulation 2 ~ 4 hours; The material flowing out from enzymatic vessel enters into pressure filter, macromole slag body is adsorbed on barrier film, small molecules material flows into the liquid storage tank of below with liquid, the described liquid through press filtration enters ion-exchanger by the pump housing, liquid after three tank bodies are to the reaction decomposes of chromium, lead and arsenic, by the pump housing, entered in concentration evaporator and concentrated, the concentrated solution after concentration evaporator is concentrated is squeezed into hig h-speed centrifugal spray drying device by pump and is made powder.
The prepared collagen product of the utility model is instant food, therefore in the whole course of processing, to strictly control microbial growth breeding, first, keep indoor environment temperature under the lower state of 10～16 ℃, secondly, before and after all Work tools are used, all will carry out water cleaning at every turn, and soak half an hour with the javelle water of 200ppm, and with tap water, clorox is rinsed well.
Collagen product detected result prepared by the utility model
Collagen product microbiological indicator prepared by the utility model
The utility model, by enzymolysis, two-stage filtration and concentrated dusting, is prepared into the collagen product that meets food sanitation standard and have nourishing function, and this automatic production line is simple in structure, is easy to control, and facility investment is few, non-environmental-pollution; In addition, the abundant raw material that the utility model adopts is easy to get, in prepared collagen product, protein content is high, and product has very strong biological activity, can be used for preparing protective foods or the medicine of anti-oxidant, hypotensive, atherosclerosis or beauty treatment.
The above-mentioned embodiment of the utility model, just illustrates, and is not only, all within the scope of the utility model or the change being equal in scope of the present utility model all by the utility model, surrounded.
Claims (6)
1. a collagen protein automatic production line, it is characterized in that: comprise service sink (1), boiling sterilization tank (2), enzyme digestion reaction tank (3), pressure filter (4), ion-exchanger (5), concentration evaporator (6) and centrifugal spray drier (7), service sink (1) is connected by travelling belt (8) with boiling sterilization tank (2), between service sink (1) and boiling sterilization tank (2), be provided with division board (9), described enzyme digestion reaction tank (3) is provided with opening for feed and discharge port, opening for feed is connected with boiling sterilization tank (2) by the pump housing, discharge port connects pressure filter (4) by the pump housing, pressure filter (4) is connected with ion-exchanger (5) by pump, ion-exchanger (5) is connected with concentration evaporator (6) by pump, described concentration evaporator (6) is connected with hig h-speed centrifugal spray drying device (7) by slush pump.
2. collagen protein automatic production line according to claim 1, is characterized in that: described enzyme digestion reaction tank (3) comprises tank body, heating unit, whipping appts, opening for feed and discharge port, and described heating unit is positioned at tank base.
3. collagen protein automatic production line according to claim 1, is characterized in that: described pressure filter (4) is hydraulic diaphragm pressure filter.
4. collagen protein automatic production line according to claim 1, is characterized in that: described ion-exchanger (5) is provided with three tank bodies, by pipeline, connects successively.
5. collagen protein automatic production line according to claim 1, is characterized in that: described concentration evaporator (6) is single-action falling film type thickener.
6. according to the collagen protein automatic production line described in claim 1 ~ 5 any one, it is characterized in that: described boiling sterilization tank (2), enzyme digestion reaction tank (3), pressure filter (4), ion-exchanger (5) and concentration evaporator (6) are equipped with automatic flushing device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320556606.4U CN203429169U (en) | 2013-09-09 | 2013-09-09 | Automatic collagen production line |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320556606.4U CN203429169U (en) | 2013-09-09 | 2013-09-09 | Automatic collagen production line |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203429169U true CN203429169U (en) | 2014-02-12 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320556606.4U Expired - Fee Related CN203429169U (en) | 2013-09-09 | 2013-09-09 | Automatic collagen production line |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203429169U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106632667A (en) * | 2017-01-12 | 2017-05-10 | 佛山科学技术学院 | Domestic integrated collagen preparation device |
| CN108485961A (en) * | 2018-06-29 | 2018-09-04 | 邱芳萍 | The production line of collagen peptide is extracted from wood frog's fallopian tube skin |
| CN109893881A (en) * | 2019-01-24 | 2019-06-18 | 舟山瑞洋水产品研发有限公司 | Ocean shrimp crab extraction process and equipment |
| CN110747120A (en) * | 2019-11-11 | 2020-02-04 | 海南勤富食品有限公司 | Environmental regulation and control system for tilapia factory |
| NL2031244A (en) * | 2021-04-04 | 2022-07-26 | Jellice Pioneer Private Ltd | System for preparing collagen tripeptide (gly-x-y) microparticles |
-
2013
- 2013-09-09 CN CN201320556606.4U patent/CN203429169U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106632667A (en) * | 2017-01-12 | 2017-05-10 | 佛山科学技术学院 | Domestic integrated collagen preparation device |
| CN108485961A (en) * | 2018-06-29 | 2018-09-04 | 邱芳萍 | The production line of collagen peptide is extracted from wood frog's fallopian tube skin |
| CN109893881A (en) * | 2019-01-24 | 2019-06-18 | 舟山瑞洋水产品研发有限公司 | Ocean shrimp crab extraction process and equipment |
| CN110747120A (en) * | 2019-11-11 | 2020-02-04 | 海南勤富食品有限公司 | Environmental regulation and control system for tilapia factory |
| NL2031244A (en) * | 2021-04-04 | 2022-07-26 | Jellice Pioneer Private Ltd | System for preparing collagen tripeptide (gly-x-y) microparticles |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140212 Termination date: 20140909 |
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| EXPY | Termination of patent right or utility model |