Enzymolysis reaction kettle

The high-temperature inactivation of enzymes is achieved by using air-dividing pipes, rotary air-tubes and air-jet pore structures in the enzymatic lysis reactor, which solves the problem of additional enzyme-destruction containers in the prior art to increase equipment costs, and ensures that the powder conveying mechanism is used to ensure that The quantitative filling of wheat flour achieves cost saving and efficiency improvement.

CN222274519UActive Publication Date: 2024-12-31WUHAN CHORTLE BIO CHEM TECH
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Patent Information

Application Number
CN202420611895.1
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-03-27
Publication Date
2024-12-31
Estimated Expiration
2034-03-27

AI Technical Summary

Technical Problem

The prior art requires the establishment of an enzyme deactivation container for enzyme inactivation of wheat protein, which increases the cost of production equipment.

Method used

An enzymatic lysis reactor was designed, using a gas pipe, a rotary air tube and a vent pore structure. The high-temperature gas is dispersed in the rotary tube to generate bubbles, achieving high-temperature inactivation of enzymes, avoiding the need for another enzyme destruction container, and at the same time, The powder conveying mechanism ensures quantitative filling of wheat flour.

Benefits of technology

There is no need to set up an enzyme destruction container, which saves production equipment costs and ensures quantitative feeding when filling wheat flour, improving production efficiency.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model discloses an enzymolysis reaction kettle which comprises a kettle tank and a powder conveying mechanism, the kettle tank is a metal tank body erected through supporting legs, a powder filling port and a plurality of water filling ports are formed in the kettle tank, the top of the kettle tank is rotationally matched with a rotating pipe of a vertical pipe structure, the top of the rotating pipe is connected with a high-temperature pipe through a rotating connector, the rotating pipe is provided with stirring paddles which are evenly distributed in the kettle tank, and a gas distributing pipe is arranged at the bottom of the rotating pipe. Rotating hollow pipes with hollow pipe body structures are arrayed on the gas distributing pipe, the rotating hollow pipes are communicated with the interior of the rotating pipe through the gas distributing pipe, and through holes which are uniformly distributed are formed in the rotating hollow pipes to form gas spraying holes; a driving mechanism for providing rotating power for the rotating pipe is arranged on the kettle tank, a discharging opening with a valve is formed in the bottom of the kettle tank, and the kettle tank is coated with a heat preservation mechanism; the method has the advantages that an enzyme deactivation container is not needed, and production equipment cost is saved; quantitative feeding can be guaranteed when wheat flour is fed.
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Description

Technical Field

[0001] The utility model belongs to the technical field of wheat protein preparation equipment, in particular to an enzymolysis reactor. Background Art

[0002] Wheat contains about 13% protein, which is mainly composed of albumin, globulin, alcohol-soluble protein and glutenin. Wheat gluten protein mainly contains gliadin and glutenin, collectively known as storage protein (accounting for 80% of wheat protein on a dry basis). Because gliadin is ductile and glutenin is elastic, they can form a network structure with water, thus having unique physical properties such as excellent viscoelasticity, extensibility, water absorption, liposuction emulsification, film forming properties and a light and mellow aroma or a slight cereal flavor.

[0003] The patent document with publication number CN102907559A discloses a prior art wheat protein enzymatic hydrolysis method: a preparation method for hydrolyzing wheat protein. In the present invention, 10 to 20 parts of papain and 5 to 10 parts of thermophilic protease are weighed and added to the interior of the reactor in step S2; trypsin is added to the mixed solution prepared in step S4, and the solution is heated and stirred. When the temperature is heated to 40°C, the mixed solution is continued to undergo a hydrolysis reaction; when the pH is adjusted to 8.5, 1.5 to 3 parts of a composite enzyme preparation are added to the system, and it is started to undergo hydrolysis. Trypsin, papain, thermophilic protease and composite enzyme preparation are added, so that in the process of hydrolyzing wheat protein, different enzymes can fully react with wheat gluten protein powder.

[0004] It can be seen that the hydrolyzed wheat protein mixture contains a large amount of biological enzymes, which must be inactivated before use. However, the existing technology requires taking out the wheat protein mixture when inactivating the enzymes and then setting up another reactor (or reaction container) to inactivate the enzymes at high temperature. The inactivation treatment cannot be performed directly in the hydrolysis reaction container, which increases the cost of production equipment. Utility Model Content

[0005] The utility model aims to provide an enzymatic hydrolysis reactor to solve the technical problem that an enzyme inactivation container is required in the above-mentioned background technology, which increases the equipment cost.

[0006] The above technical objectives of the utility model are achieved through the following technical solutions:

[0007] An enzymatic hydrolysis reactor comprises: a kettle and a powder conveying mechanism; the kettle is a metal tank body elevated by a support leg, a powder filling port and a plurality of water filling ports are arranged on the kettle, a rotating tube with a vertical pipe structure is rotatably matched at the top of the kettle, a high-temperature tube is connected to the top of the rotating tube through a rotating joint, a stirring paddle evenly distributed inside the kettle is arranged on the rotating tube, an air distribution pipe is arranged at the bottom of the rotating tube, a rotating empty tube with a hollow tube structure is arranged on the air distribution pipe, the rotating empty tube is connected to the inside of the rotating tube through the air distribution pipe, and evenly distributed through holes are arranged on the rotating empty tube to form air jet holes; a driving mechanism for providing rotational power for the rotating tube is arranged on the kettle, a discharge port with a valve is arranged at the bottom of the kettle, and a heat preservation mechanism is coated on the outside of the kettle.

[0008] Furthermore, in order to maintain the enzymatic hydrolysis temperature, the insulation mechanism includes: a hot inlet, a cold outlet, a covering shell, and a heat exchange chamber; the outer covering of the covering shell is included outside the outer shell of the kettle tank, a gap is provided between the covering shell and the outer shell of the kettle tank to form a heat exchange chamber, and a support is provided inside the heat exchange chamber to connect the covering shell and the kettle tank; the covering shell is provided with two pipeline interfaces and the inside of the heat exchange chamber is connected to the hot inlet and the cold outlet respectively.

[0009] Furthermore, in order to increase the length of the heat exchange process, the hot inlet and the cold outlet are arranged on non-same sides in the direction of the covering shell.

[0010] Furthermore, in order to provide rotational power for the rotating tube, the driving mechanism includes: a motor, a reducer, a driving wheel, and a driven wheel; a reducer is fixed to the top of the kettle through a bracket, the input end of the reducer and the output end of the motor are coaxially fixed, the motor is fixed on the reducer housing, a driving wheel is fixed to the output shaft of the reducer, and the rotating tube is provided with a driven wheel at the same height as the driving wheel, and the driving wheel and the driven wheel are connected by a chain or belt drive.

[0011] Furthermore, in order to facilitate the installation of auxiliary mechanisms and to enhance the strength of the kettle, a reinforcing hoop frame with a frame structure is provided on the outer hoop of the kettle.

[0012] Furthermore, in order to facilitate the transportation of wheat flour, a powder conveying mechanism is provided at the powder filling port, and the powder conveying mechanism includes: a powder feed port, a lower inflection, a lifting pipe, and a discharge branch pipe; the lifting pipe is an inclined straight pipe, and the lifting pipe is fixed to the reinforcing hoop frame by a plurality of hangers; the lowest position of the lifting pipe is connected to a pipe through a lower inflection of a curved pipe structure, and the end of the pipe is the powder feed port, and an end of the lifting pipe away from the lower inflection is provided with a discharge branch pipe extending toward the powder filling port, and the lower end of the discharge branch pipe is located directly above the powder filling port.

[0013] Furthermore, in order to ensure quantitative feeding when adding wheat flour, a propeller is built into the lifting pipe, the upper port of the propeller is located above the discharge branch pipe, and a lifting motor is fixed to the upper end of the lifting pipe, and the output end of the lifting motor is coaxially connected to the propeller.

[0014] Furthermore, in order to facilitate monitoring of the hydrolysis temperature and the temperature during enzyme inactivation in the kettle, a thermometer is fixed on the top of the kettle, and the temperature detection probe of the thermometer is located inside the kettle.

[0015] In summary, the utility model has the following beneficial effects:

[0016] ① No need to set up a separate enzyme inactivation container, saving production equipment costs: through the establishment of the gas distribution pipe, the rotating empty pipe, the air jet hole, and the rotating joint, when the wheat protein turbid liquid is inactivated, there is no need to set up a separate enzyme inactivation container. The high-temperature gas directly enters the rotating tube through the high-temperature pipe and is transmitted to the gas distribution pipe at the lower end of the rotating tube. The gas distribution pipe disperses the high-temperature airflow to each group of rotating empty pipes. The rotating empty pipe disperses the airflow to each group of air jet holes. The air jet holes spray the high-temperature airflow to generate a large number of high-temperature bubbles, and these high-temperature bubbles are dispersed under the rotation of the rotating tube to be evenly distributed in the kettle. The high-temperature bubbles contact the water in the kettle to generate a large amount of high-temperature steam, which inactivates the enzyme in the water at high temperature to complete the enzyme inactivation process. No separate enzyme inactivation container is needed, saving production equipment costs.

[0017] ② It can ensure quantitative feeding when adding wheat flour: through the establishment of the powder conveying mechanism, the lifting motor in the powder conveying mechanism drives the propeller to rotate, and the propeller lifts the wheat flour at the lower inflection point and conveys it to the lifting pipe, and then discharges it to the powder filling port through the discharge branch pipe. By setting the working time of the motor, the amount of wheat flour added is determined, thereby ensuring quantitative feeding of wheat flour. BRIEF DESCRIPTION OF THE DRAWINGS

[0018] Figure 1 It is a schematic diagram of the overall structure of the utility model;

[0019] Figure 2 It is a schematic diagram of the top view structure of the utility model;

[0020] Figure 3 It is a schematic diagram of the internal structure of the utility model;

[0021] Figure 4 yes Figure 3 A magnified view of the structure in the middle;

[0022] Figure 5 yes Figure 3 A magnified view of the structure at B in the middle;

[0023] Figure 6It is a structural schematic diagram of the wheat flour feeding mechanism in the utility model;

[0024] In the figure, 1, kettle; 2, water filling port; 3, powder filling port; 4, high temperature pipe; 5, driving mechanism; 6, rotating pipe; 7, powder conveying mechanism; 8, rotating joint; 9, insulation mechanism; 10, support leg; 11, discharge port; 12, thermometer; 13, reinforcing hoop frame; 14, stirring paddle; 15, hanger; 51, motor; 52, reducer; 53, driving wheel; 54, driven wheel; 61, air distribution pipe; 62, rotating empty pipe; 63, jet hole; 71, powder feeding port; 72, lower inflection; 73, lifting pipe; 74, discharge branch pipe; 75, propeller; 76, lifting motor; 91, hot inlet; 92, cold outlet; 93, covering shell; 94, heat exchange chamber. DETAILED DESCRIPTION

[0025] The utility model is further described in detail below in conjunction with the accompanying drawings.

[0026] Example:

[0027] See also Figure 1-Figure 6 , the utility model provides a technical solution:

[0028] An enzymatic hydrolysis reactor comprises: a kettle 1 and a powder conveying mechanism 7; the kettle 1 is a metal tank body elevated by legs 10, a powder filling port 3 and a plurality of water filling ports 2 are provided on the kettle 1, a rotating tube 6 with a vertical tube structure is rotatably matched at the top of the kettle 1, a high-temperature tube 4 is connected to the top of the rotating tube 6 through a rotating joint 8, a stirring paddle 14 evenly distributed inside the kettle 1 is provided with the rotating tube 6, a gas distribution pipe 61 is provided at the bottom of the rotating tube 6, a rotating empty tube 62 with a hollow tube structure is arrayed on the gas distribution pipe 61, the rotating empty tube 62 is connected to the inside of the rotating tube 6 through the gas distribution pipe 61, and the rotating empty tube 62 is provided with evenly distributed through holes to form an air jet hole 63; a driving mechanism 5 for providing rotational power for the rotating tube 6 is provided on the kettle 1, a discharge port 11 with a valve is provided at the bottom of the kettle 1, and a heat preservation mechanism 9 is coated on the outside of the kettle 1.

[0029] The heat preservation mechanism 9 includes: a heat inlet 91, a cold outlet 92, a covering shell 93, and a heat exchange chamber 94; the covering shell 93 is covered on the outside of the outer shell of the kettle 1, and a gap is provided between the covering shell 93 and the outer shell of the kettle 1 to form a heat exchange chamber 94, and a support is provided inside the heat exchange chamber 94 to connect the covering shell 93 and the kettle 1; the covering shell 93 is provided with two pipeline interfaces and the inside of the heat exchange chamber 94 is connected to the heat inlet 91 and the cold outlet 92 respectively.

[0030] The heat inlet 91 and the cold outlet 92 are arranged on different sides of the covering shell 93 .

[0031] The driving mechanism 5 includes: a motor 51, a reducer 52, a driving wheel 53, and a driven wheel 54; a reducer 52 is fixed to the top of the kettle 1 through a bracket, the input end of the reducer 52 and the output end of the motor 51 are coaxially fixed, the motor 51 is fixed on the outer shell of the reducer 52, and a driving wheel 53 is fixed to the output shaft of the reducer 52. The rotating tube 6 is provided with a driven wheel 54 at the same height as the driving wheel 53, and the driving wheel 53 and the driven wheel 54 are connected by a chain or belt transmission.

[0032] The kettle 1 is provided with a reinforcing hoop frame 13 of a frame structure on the outer hoop.

[0033] A powder conveying mechanism 7 is provided at the powder filling port 3, and the powder conveying mechanism 7 includes: a powder feeding port 71, a lower inflection port 72, a lifting pipe 73, and a discharge branch pipe 74; the lifting pipe 73 is an inclined straight pipe, and the lifting pipe 73 is fixed to the reinforcing hoop frame 13 by a plurality of hangers 15 (for the sake of simplicity of the drawing, only one group of hangers 1 is shown in the figure); the lowest position of the lifting pipe 73 is connected to a pipeline through a lower inflection port 72 of a curved pipe structure, and the end of the pipeline is the powder feeding port 71, and the end of the lifting pipe 73 away from the lower inflection port 72 is provided with a discharge branch pipe 74 extending toward the powder filling port 3, and the lower end of the discharge branch pipe 74 is located directly above the powder filling port 3.

[0034] In order to ensure quantitative addition when adding wheat flour (this quantitative addition is interval quantitative addition rather than precise quantitative addition), a propeller 75 is built into the lifting pipe 73, and the upper port of the propeller 75 is located above the discharge branch pipe 74. A lifting motor 76 is fixed to the upper end of the lifting pipe 73, and the output end of the lifting motor 76 is coaxially connected to the propeller 75.

[0035] A thermometer 12 is fixed on the top of the kettle 1 , and a temperature detection probe of the thermometer 12 is located inside the kettle 1 .

[0036] Brief description of the usage process:

[0037] When in use, the motor 51 and the lifting motor 76 are connected to an external power supply with a switch, the heat inlet 91 is connected to a heat source gas circuit or a heat source water circuit with a valve, the cold outlet 92 is connected to a recovery pipeline, and the high-temperature pipe 4 is used to fix the high-temperature gas pipe with a valve;

[0038] The flour feeding port 71 is used to connect the flour conveying pipeline. Due to the weight, the flour will accumulate at the lower inflection point 72. Since the propeller 75 is provided in the lifting pipe 73, the lifting pipe 73 will be sealed in disguise. The flour at the lower inflection point 72 cannot directly enter the upper part of the lifting pipe 73.

[0039] Then, the lifting motor 76 is started to rotate, and the lifting motor 76 drives the propeller 75 to rotate. The propeller 75 lifts the wheat flour at the lower inflection 72 and transports it to the lifting pipe 73, and then discharges it to the powder filling port 3 through the discharge branch pipe 74. The amount of wheat flour added is determined by setting the working time of the motor 76 (the amount of wheat flour added is proportional to the working time of the motor 76, and the amount of wheat flour added can be calculated by the single-hour delivery amount), and then water and reaction enzyme liquid are added through the water filling port 2;

[0040] Then, the valve with the heat inlet 91 is opened, and the heat inlet 91 delivers the heat source to the heat exchange chamber 94, and the heat exchange chamber 94 and the kettle 1 perform heat exchange, raising the temperature in the kettle 1 to the enzymolysis temperature;

[0041] Then the motor 51 is started to rotate, and the motor 51 drives the driving wheel 53 to rotate through the reducer, and the driving wheel 53 drives the driven wheel 54 and the rotating tube 6 to rotate as a whole, and then the stirring paddle 14 on the rotating tube 6 rotates to mix the wheat flour, water and enzyme solution, and under the support of the heat preservation mechanism 9, the wheat flour undergoes a hydrolysis reaction to form hydrolyzed wheat protein. After a period of reaction, a turbid liquid containing hydrolyzed wheat protein is formed in the kettle 1. At this time, the turbid liquid needs to be enzyme-inactivated and then discharged for the next step;

[0042] When inactivating the enzyme, the valve at the high-temperature tube 4 is opened, and the high-temperature gas enters the rotating tube 6 from the high-temperature tube 4 and is transmitted to the gas distribution pipe 61 at the lower end of the rotating tube 6. The gas distribution pipe 61 disperses the high-temperature airflow to each group of rotating empty tubes 62. The rotating empty tubes 62 disperse the airflow to each group of air jet holes 63. The air jet holes 63 spray out the high-temperature airflow to generate a large number of high-temperature bubbles, and these high-temperature bubbles are dispersed under the rotation of the rotating tube 6 to be evenly distributed in the kettle 1. The high-temperature bubbles contact the water in the kettle 1 to generate a large amount of high-temperature steam, which inactivates the enzyme in the water at high temperature and completes the enzyme inactivation process. After the enzyme inactivation process is completed, the turbid liquid is sent from the discharge port 11 to the next centrifugal process to centrifuge the wheat protein.

[0043] The specific embodiments are merely explanations of the present invention and are not limitations of the present invention. After reading this specification, those skilled in the art may make modifications to the embodiments without any creative contribution as needed. However, as long as they are within the scope of the claims of the present invention, they are protected by the patent law.

Claims

1. An enzymatic hydrolysis reactor, comprising: A kettle (1) and a powder conveying mechanism (7); characterized in that: the kettle (1) is a metal tank body elevated by legs (10); a powder filling port (3) and a plurality of water filling ports (2) are provided on the kettle (1); a rotating tube (6) with a vertical tube structure is rotatably matched at the top of the kettle (1); a high-temperature tube (4) is connected to the top of the rotating tube (6) via a rotating joint (8); the rotating tube (6) is provided with evenly distributed stirring paddles (14) inside the kettle (1); and the bottom of the rotating tube (6) is provided with a stirring paddle (14) arranged on the bottom of the rotating tube (6). A gas distribution pipe (61) is provided, and a rotating hollow pipe (62) with a hollow tube structure is arranged on the gas distribution pipe (61), and the rotating hollow pipe (62) is connected through the gas distribution pipe (61) and the inside of the rotating pipe (6), and the rotating hollow pipe (62) is provided with evenly distributed through holes to form a gas injection hole (63); a driving mechanism (5) for providing a rotating power for the rotating pipe (6) is provided on the kettle (1), and a discharge port (11) with a valve is provided at the bottom of the kettle (1), and the kettle (1) is covered with a heat preservation mechanism (9).

2. An enzymatic hydrolysis reactor according to claim 1, characterized in that: The heat preservation mechanism (9) comprises: a heat inlet (91), a cold outlet (92), a covering shell (93), and a heat exchange chamber (94); the covering shell (93) is covered on the outside of the outer shell of the kettle (1); a gap is provided between the covering shell (93) and the outer shell of the kettle (1) to form a heat exchange chamber (94); a support is provided inside the heat exchange chamber (94) to connect between the covering shell (93) and the kettle (1); the covering shell (93) is provided with two pipeline interfaces and the inside of the heat exchange chamber (94) are connected to the heat inlet (91) and the cold outlet (92), respectively.

3. An enzymatic hydrolysis reactor according to claim 2, characterized in that: The heat inlet (91) and the cold outlet (92) are arranged on non-coplanar sides of the covering shell (93).

4. An enzymatic hydrolysis reactor according to claim 1, characterized in that: The driving mechanism (5) comprises: a motor (51), a reducer (52), a driving wheel (53), and a driven wheel (54); a reducer (52) is fixed to the top of the kettle (1) through a bracket, the input end of the reducer (52) and the output end of the motor (51) are coaxially fixed, the motor (51) is fixed on the housing of the reducer (52), a driving wheel (53) is fixed to the output shaft of the reducer (52), and the rotating tube (6) is provided with a driven wheel (54) at the same height as the driving wheel (53), and the driving wheel (53) and the driven wheel (54) are connected by a chain or a belt transmission.

5. An enzymatic hydrolysis reactor according to claim 1, characterized in that: The kettle (1) is provided with a reinforcing hoop frame (13) of frame structure on the outer hoop.

6. An enzymatic hydrolysis reactor according to claim 5, characterized in that: A powder conveying mechanism (7) is provided at the powder filling port (3), and the powder conveying mechanism (7) comprises: a powder feeding port (71), a lower inflection port (72), a lifting pipe (73), and a discharge branch pipe (74); the lifting pipe (73) is an inclined straight pipe, and the lifting pipe (73) is fixed to the reinforcing hoop frame (13) by means of a plurality of hangers (15); the lowest position of the lifting pipe (73) is connected to a pipeline through a lower inflection port (72) of a curved pipe structure, and the end of the pipeline is the powder feeding port (71); an end of the lifting pipe (73) away from the lower inflection port (72) is provided with a discharge branch pipe (74) extending toward the powder filling port (3), and the lower end of the discharge branch pipe (74) is located directly above the powder filling port (3).

7. An enzymatic hydrolysis reactor according to claim 6, characterized in that: A propeller (75) is built into the lifting pipe (73), and the upper end of the propeller (75) is located above the discharge branch pipe (74). A lifting motor (76) is fixed to the upper end of the lifting pipe (73), and the output end of the lifting motor (76) is coaxially connected to the propeller (75).

8. An enzymatic hydrolysis reactor according to claim 1, characterized in that: A thermometer (12) is fixed on the top of the kettle (1), and a temperature detection probe of the thermometer (12) is located inside the kettle (1).