CN214382177U - Continuous type plant pulp enzymolysis system - Google Patents
Continuous type plant pulp enzymolysis system Download PDFInfo
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- CN214382177U CN214382177U CN202023297439.5U CN202023297439U CN214382177U CN 214382177 U CN214382177 U CN 214382177U CN 202023297439 U CN202023297439 U CN 202023297439U CN 214382177 U CN214382177 U CN 214382177U
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Abstract
The utility model relates to a continuous type plant pulp enzymolysis system. The system comprises a liquid supply pump (1), an enzymolysis heating pipeline (2), an enzymolysis constant-temperature pipeline (3), an enzyme deactivation heating pipeline (4) and an enzyme deactivation constant-temperature pipeline (5). Through the length of the pipeline and the pump speed regulation of the conveyed materials, the heating time and the constant temperature time of the enzymolysis process are regulated, the consistency of the enzymolysis parameters of the materials can be realized, in addition, the enzymolysis degree can be accurately regulated, and the production and processing of grain beverages with different viscosities can be realized.
Description
Technical Field
The utility model relates to a beverage processing technology field, and in particular to plant beverage's processing technology.
Background
Oats are one of crops with the highest nutritional value in cereals, have the characteristics of high protein, high unsaturated fatty acid, high beta-glucan and the like, have been widely accepted for preventing and treating cardiovascular and cerebrovascular diseases caused by hyperlipidemia, controlling blood sugar of a human body, losing weight and the like, and the American Food and Drug Administration (FDA) publishes the function of reducing heart disease risk of oats in 1997.
The grain beverage processing is a new direction of grain processing, compared with other grains, the oat contains more beta-glucan and fat, and the characteristics endow the oat with better emulsification characteristic and special aroma, thereby laying a certain material foundation for developing oat beverage products.
Traditionally, the raw material is enzymolyzed in an enzymolysis tank. The slurry mixed with the enzyme preparation is conveyed into an enzymolysis tank, then the temperature is raised to the enzymolysis temperature and the constant temperature is kept for a certain time, and then the slurry is conveyed into an enzyme deactivation tank for heating and enzyme deactivation. Because the tank body has a certain volume, the time difference of feeding and discharging materials in the same tank can be caused, and the enzymolysis degree of the materials fed and discharged in sequence is different. In addition, the business turn over of material needs to consume certain time in the jar body, and this to some quick enzymolysis reaction of speed, can cause complete enzymolysis, and this makes and can not realize the accurate control to the enzymolysis degree.
SUMMERY OF THE UTILITY MODEL
In order to solve the technical problem, the utility model designs a plant pulp enzymolysis system of one set of continuous type, specific technical scheme is as follows:
the utility model provides a continuous type plant thick liquids enzymolysis system, its characterized in that includes feed pump (1), enzymolysis heating pipeline (2), enzymolysis constant temperature pipeline (3), goes out enzyme heating pipeline (4), goes out enzyme constant temperature pipeline (5), after plant thick liquids and enzyme preparation mix, by feed pump (1) carry extremely enzymolysis heating pipeline (2) heat up to the enzymolysis temperature, then enter into constant temperature carries out the enzymolysis in enzymolysis constant temperature pipeline (3), then enters into go out enzyme heating pipeline (4) heat up to going out enzyme temperature, and the last material enters into go out enzyme constant temperature pipeline (5) constant temperature goes out the enzyme.
Further, the liquid supply pump (1) comprises one or a combination of two or more of a rotor pump, a centrifugal pump, a screw pump and a diaphragm pump.
Further, the enzymolysis heating pipeline (2) and the enzyme deactivation heating pipeline (4) are in a coil form and are immersed in constant-temperature liquid to realize temperature rise.
Further, the enzymolysis heating pipeline (2) and the enzyme deactivation heating pipeline (4) are in the form of a sleeve heat exchanger.
Furthermore, the outer walls of the enzymolysis constant-temperature pipeline (3) and the enzyme-inactivating constant-temperature pipeline (5) are coated with heat-insulating layers to realize constant temperature.
Further, still include the thermometer, the thermometer sets up enzymolysis heating tube says (2), enzymolysis constant temperature pipeline (3), enzyme deactivation heating tube says (4), goes out different positions of enzyme constant temperature pipeline (5) for the thick liquids temperature in the monitoring pipeline carries out control.
Furthermore, the enzyme deactivation constant temperature pipeline device further comprises a backpressure valve, and the backpressure valve is arranged at the outlet end of the enzyme deactivation constant temperature pipeline (5).
Further, the plant pulp comprises: one or more of rice, wheat, oat, buckwheat, barley, highland barley, corn, sorghum, millet and millet.
Further, the enzyme preparation comprises: one or the combination of two or more of amylase, protease, cellulase and saccharifying enzyme.
The utility model discloses a but pipeline of continuous transport material can adjust the heat time and the constant temperature time of enzymolysis process through the length of pipeline and the pump speed of transported substance material, and this makes the enzymolysis parameter that whole materials passed through all unified, has avoided the enzymolysis degree difference problem of the front and back feeding that batch formula enzymolysis treatment brought.
In addition, because the enzymolysis time can be accurately controlled, the control of the enzymolysis degree can also be realized. Particularly for some enzyme preparations with short enzymolysis time, such as amylase and the like, the batch type treatment traditionally leads the enzymolysis degree to complete enzymolysis due to the long time of feeding and discharging. Thus, for some cereal materials, the viscosity is reduced too much, resulting in a beverage product that tastes thin and lacks a food sensation. And the utility model discloses a continuous type enzymolysis system can be through adjusting from the enzymolysis to the time of enzyme deactivation, to the accurate regulation of enzymolysis degree, can realize the production and processing of the cereal beverage of different viscosities.
Drawings
Fig. 1 is a continuous plant pulp enzymolysis system in example 1, wherein 1 is a liquid feed pump, 2 is an enzymolysis heating pipeline, 3 is an enzymolysis constant temperature pipeline, 4 is an enzyme deactivation heating pipeline, and 5 is an enzyme deactivation constant temperature pipeline.
Detailed Description
Example 1
The utility model provides a continuous type oat thick liquids enzymolysis system which characterized in that includes feed pump 1, enzymolysis heating tube 2, enzymolysis constant temperature pipeline 3, enzyme deactivation heating tube 4, enzyme deactivation constant temperature pipeline 5. The liquid supply pump 1 is a screw pump. Enzymolysis heating pipeline 2 with enzyme deactivation heating pipeline 4 is the coil form, and wherein enzymolysis heating pipeline 2 submergence realizes rising temperature in homothermal aquatic, and enzymolysis heating pipeline 4 submergence realizes rising temperature in homothermal aquatic. The enzymolysis constant temperature pipeline 3 with the outer wall cladding of the pipeline of enzyme deactivation constant temperature pipeline 5 has the heat preservation to realize the constant temperature. The inlet and the outlet of the enzymolysis heating pipeline 2, the enzymolysis constant temperature pipeline 3, the enzyme deactivation heating pipeline 4 and the enzyme deactivation constant temperature pipeline 5 are respectively provided with a thermometer for detecting the temperature of the materials in the pipelines. The outlet of the enzyme-inactivating constant-temperature pipeline 5 is also provided with a backpressure valve to realize pressure maintaining in the whole pipeline.
After being mixed with an amylase preparation, the oat slurry is conveyed to an enzymolysis heating pipeline 2 by a liquid supply pump 1, the temperature is raised to 65 ℃ of enzymolysis temperature, then the oat slurry enters an enzymolysis constant-temperature pipeline 3, the enzymolysis is carried out for 2 minutes at constant temperature, then the oat slurry enters an enzyme deactivation heating pipeline 4, the temperature is raised to 95 ℃ of enzyme deactivation temperature, and finally the material enters an enzyme deactivation constant-temperature pipeline 5, the constant temperature is kept for 10 minutes, and enzyme deactivation is carried out. After the oat pulp is subjected to enzymolysis, the viscosity of the oat pulp is reduced from 1000cp to about 20cp-100cp (61#/100 rpm). According to the length of the enzymolysis constant-temperature pipeline 3, the enzymolysis constant-temperature time can be adjusted to realize different enzymolysis degrees, so that a product with specified viscosity can be produced.
The embodiments of the present invention have been described in detail, but the embodiments are merely examples for easy understanding and explanation, and should not be construed as limitations of the present invention. Any person skilled in the art can implement the preferred embodiments according to the technical solution of the present invention, but all such modifications belong to the scope of the claims of the present invention.
Claims (9)
1. The utility model provides a continuous type plant thick liquids enzymolysis system, its characterized in that includes feed pump (1), enzymolysis heating pipeline (2), enzymolysis constant temperature pipeline (3), goes out enzyme heating pipeline (4), goes out enzyme constant temperature pipeline (5), after plant thick liquids and enzyme preparation mix, by feed pump (1) carry extremely enzymolysis heating pipeline (2) heat up to the enzymolysis temperature, then enter into constant temperature carries out the enzymolysis in enzymolysis constant temperature pipeline (3), then enters into go out enzyme heating pipeline (4) heat up to going out enzyme temperature, and the last material enters into go out enzyme constant temperature pipeline (5) constant temperature goes out the enzyme.
2. The enzymatic hydrolysis system of claim 1, wherein: the liquid supply pump (1) comprises one or the combination of two or more of a rotor pump, a centrifugal pump, a screw pump and a diaphragm pump.
3. The enzymatic hydrolysis system of claim 1, wherein: the enzymolysis heating pipeline (2) and the enzyme deactivation heating pipeline (4) are in a coil form and are immersed in constant-temperature liquid to realize temperature rise.
4. The enzymatic hydrolysis system of claim 1, wherein: the enzymolysis heating pipeline (2) and the enzyme deactivation heating pipeline (4) are in the form of a sleeve heat exchanger.
5. The enzymatic hydrolysis system of claim 1, wherein: the enzymolysis constant temperature pipeline (3) and the outer wall of the enzyme-inactivating constant temperature pipeline (5) are coated with heat-insulating layers to realize constant temperature.
6. The enzymolysis system of claim 1, characterized in that further comprises thermometers, the thermometers are arranged at different positions of the enzymolysis heating pipeline (2), the enzymolysis constant temperature pipeline (3), the enzyme deactivation heating pipeline (4) and the enzyme deactivation constant temperature pipeline (5), and are used for monitoring and controlling the temperature of the slurry in the pipelines.
7. The enzymolysis system of claim 1, characterized in that further comprises a back pressure valve, said back pressure valve is disposed at the outlet end of said enzyme deactivation thermostatic conduit (5).
8. The enzymatic hydrolysis system as set forth in claim 1, wherein said plant pulp includes: one of rice, wheat, oat, buckwheat, barley, highland barley, corn, sorghum, millet and millet.
9. The enzymatic system of claim 1, wherein said enzyme preparation comprises: amylase, protease, cellulase, and saccharifying enzyme.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202023297439.5U CN214382177U (en) | 2020-12-31 | 2020-12-31 | Continuous type plant pulp enzymolysis system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202023297439.5U CN214382177U (en) | 2020-12-31 | 2020-12-31 | Continuous type plant pulp enzymolysis system |
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| CN214382177U true CN214382177U (en) | 2021-10-12 |
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| CN202023297439.5U Active CN214382177U (en) | 2020-12-31 | 2020-12-31 | Continuous type plant pulp enzymolysis system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP4342300A1 (en) * | 2022-09-21 | 2024-03-27 | frischli Milchwerke GmbH | Method for producing at least one plant-based beverage and device for producing at least one plant-based beverage |
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2020
- 2020-12-31 CN CN202023297439.5U patent/CN214382177U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP4342300A1 (en) * | 2022-09-21 | 2024-03-27 | frischli Milchwerke GmbH | Method for producing at least one plant-based beverage and device for producing at least one plant-based beverage |
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