Multi-section enzymolysis reaction device

By introducing stirring, primary heating and fine heating structures into the enzymatic hydrolysis reaction device, the problem of poor enzymatic hydrolysis temperature control is solved and the optimal enzymatic hydrolysis effect is achieved.

CN223433483UActive Publication Date: 2025-10-14WUHAN CHORTLE BIO CHEM TECH
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Patent Information

Application Number
CN202422806493.X
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-11-15
Publication Date
2025-10-14
Estimated Expiration
2034-11-15

AI Technical Summary

Technical Problem

The enzymatic hydrolysis reaction device in the prior art cannot effectively control the enzymatic hydrolysis temperature, resulting in poor enzymatic hydrolysis effect.

Method used

A multi-stage enzymatic hydrolysis reaction device is designed, which includes a mixing tank, a mixing element and a collecting element. The mixing element includes a stirring element, a primary heating element and a fine heating element. The stirring element stirs the material evenly in the first chamber, the primary heating element performs preliminary heating on the material, and the fine heating element performs temperature-controlled heating to ensure that the material reaches the optimal enzymatic hydrolysis temperature.

Benefits of technology

By precisely controlling the enzymatic hydrolysis temperature, the optimal enzymatic hydrolysis effect is achieved, and the efficiency and effect of the enzymatic hydrolysis reaction are improved.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model relates to a multistage enzymolysis reaction device which comprises a mixing tank body, a mixing piece and a collecting piece, and the mixing tank body is provided with a first chamber and a second chamber; the mixing part comprises a stirring part, a primary heating part and a fine heating part, and the stirring part is rotationally connected into the first cavity; the initial heating piece is arranged in the second cavity; the fine heating piece is connected with the first chamber and can perform temperature-controlled heating on the to-be-enzymolyzed material which is uniformly mixed in the first chamber; and the collecting piece is connected with the fine heating piece. The technical scheme provided by the utility model has the beneficial technical effects that the stirring part and the initial heating part of the mixing part are arranged in the first chamber of the mixing tank body; when the stirring part uniformly stirs the materials to be subjected to enzymolysis, the primary heating part is used for primarily heating the materials to be subjected to enzymolysis, so that the materials to be subjected to enzymolysis are fully mixed. And after the materials are fully mixed, the materials to be subjected to enzymolysis reach the optimal enzymolysis temperature by utilizing the fine heating piece, so that the optimal enzymolysis effect is achieved. The problems that in the prior art, the enzymolysis temperature cannot be well controlled, and the enzymolysis effect is poor are solved.
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Description

Technical Field

[0001] The utility model relates to the technical field of enzymolysis, in particular to a multi-stage enzymolysis reaction device. Background Art

[0002] Most enzymes are proteins and act as biocatalysts. Specific enzymes can catalyze specific chemical reactions, accelerating them and reducing the activation of reactants. They are often used in the preparation of small-molecule peptides due to their high catalytic efficiency, strong specificity, and mild reaction conditions, without excessive contamination that could interfere with the reaction.

[0003] Enzymatic hydrolysis, also known as enzymolysis, is a biochemical process that uses specific enzymes to break down organic matter into smaller organic or inorganic compounds. It refers to the process where a biocatalyst catalyzes the breakdown of specific organic matter into new organic matter.

[0004] Enzymes accelerate or promote chemical reactions by reducing or increasing the activity of reactants. In enzymatic reactions, enzymes do not directly participate in the reaction, but provide a catalytic environment that makes it easier for reactants to be converted into products.

[0005] Modern biomanufacturing is developing rapidly towards high intensity, intensiveness and flexibility, which places higher demands on reaction processes, production intensity and operational flexibility.

[0006] The prior art CN107974404A provides an enzymatic hydrolysis reactor. By installing a filter rod at the bottom outlet, the discharge liquid can be filtered during the discharge process. There is no need to transport the liquid to a filter tank for filtration and then return the filtered enzyme to the reactor, thus reducing enzyme waste. The enzymatic hydrolysis effect is closely related to the temperature. If the temperature does not reach the optimal enzymatic hydrolysis effect, the enzymatic hydrolysis effect will also be affected.

[0007] Therefore, it is very necessary to provide a multi-stage enzymatic hydrolysis reaction device to solve the above technical problems. Utility Model Content

[0008] Based on the above description, the present invention provides a multi-stage enzymatic hydrolysis reaction device to solve the problem that the prior art cannot well control the enzymatic hydrolysis temperature, resulting in poor enzymatic hydrolysis effect.

[0009] The technical solution of the utility model for solving the above-mentioned technical problems is as follows: a multi-stage enzymatic hydrolysis reaction device, comprising a mixing tank body, a mixing element and a collecting element, wherein the mixing tank body is provided with a first chamber and a second chamber; the mixing element comprises a stirring element, a primary heating element and a fine heating element, the stirring element is rotatably connected to the first chamber, and can stir the material to be enzymatically hydrolyzed in the first chamber evenly; the primary heating element is arranged in the second chamber, and can heat the first chamber; the fine heating element is connected to the first chamber, and can temperature-control and heat the material to be enzymatically hydrolyzed that is evenly mixed in the first chamber; the collecting element is connected to the fine heating element, and can collect the enzymatically hydrolyzed material.

[0010] In some embodiments, the stirring member includes a stirring motor, a motor gear, an upper transmission gear, a transmission rod, a lower transmission gear, a stirring gear and an agitator. The stirring motor is provided with a fixed end and a rotating end. The fixed end of the stirring motor is connected to the mixing tank body; the motor gear is connected to the rotating end of the stirring motor; the upper transmission gear is engaged with the motor gear; the transmission rod is passed through the mixing tank body, the upper end of the transmission rod is connected to the upper transmission gear, and the middle part of the transmission rod is rotatably connected to the mixing tank body; the lower transmission gear is connected to the lower end of the transmission rod; the stirring gear is rotatably connected to the mixing tank body, and the stirring gear is engaged with the lower transmission gear; the agitator is connected to the stirring gear.

[0011] In some embodiments, a bearing member is further included, wherein the outer ring of the bearing member is connected to the mixing tank body, and the inner ring of the bearing member is connected to the transmission rod.

[0012] In some embodiments, the fine heating element includes a heating water tank, a support cylinder, a spiral tube, a spiral tube pump, an outer ring heating jacket, an outer inlet and outlet water pipe, an outer water pump, an inner ring heating jacket, an inner inlet and outlet water pipe and an inner water pump, the support cylinder is connected to one side of the heating water tank; the spiral tube is connected to the support cylinder, and the feed end of the spiral tube is connected to the mixing tank body; the spiral tube pump is connected to one side of the spiral tube and can pump the material to be enzymatically hydrolyzed in the mixing tank body into the spiral tube; one side of the outer ring heating jacket is connected to the support cylinder, and the other side of the outer ring heating jacket is connected to the spiral tube ; The middle part of the outer inlet and outlet water pipes is connected to the outer ring heating jacket, and the two ends of the outer inlet and outlet water pipes are connected to the heating water tank; the outer water pump is connected to the outer inlet and outlet water pipes, and can pump the water from the heating water tank into the outer ring heating jacket; the inner ring heating jacket is connected to the inner ring of the spiral tube, and the two ends of the inner ring heating jacket are connected to the heating water tank; the middle part of the inner inlet and outlet water pipes is connected to the inner ring heating jacket, and the two ends of the inner inlet and outlet water pipes are connected to the heating water tank; the inner water pump is connected to the inner inlet and outlet water pipes, and can pump the water from the heating water tank into the inner ring heating jacket.

[0013] In some embodiments, the system further includes an external temperature sensor and an internal temperature sensor, wherein the external temperature sensor is connected to the outside of the spiral tube; and the internal temperature sensor is connected to the inside of the spiral tube.

[0014] In some embodiments, the collecting member includes a collecting tank, at least one of which is provided, and the collecting tank is connected to the discharge end of the spiral tube.

[0015] In some embodiments, the collecting member further includes a filter and a valve body, the filter is connected to the feed end of the collecting tank; the inlet end of the valve body is connected to the discharge end of the spiral tube, and the outlet end of the valve body is connected to the filter.

[0016] In some embodiments, the mixing tank is connected to a feeding end for the material to be enzymatically hydrolyzed and an acid and alkali solution addition end.

[0017] In some embodiments, a pH detector and a liquid level sensor are provided in the mixing tank.

[0018] In some embodiments, a display is provided on the mixing tank body, and the display is electrically connected to the pH value detector and the liquid level sensor, and can display the liquid level height and pH value of the material to be enzymatically hydrolyzed in the mixing tank body.

[0019] Compared with the prior art, the technical solution of this application has the following beneficial technical effects:

[0020] The stirring element and the primary heating element of the mixing unit are disposed within the first chamber of the mixing tank. While the stirring element uniformly stirs the material to be hydrolyzed, the primary heating element preliminarily heats the material to be hydrolyzed, ensuring thorough mixing. After thorough mixing, the final heating element brings the material to the optimal hydrolysis temperature, thereby achieving the best hydrolysis effect. This solves the problem of poor hydrolysis temperature control in the prior art, which results in poor hydrolysis results. BRIEF DESCRIPTION OF THE DRAWINGS

[0021] Figure 1 A schematic diagram of the overall structure of a multi-stage enzymatic hydrolysis reaction device provided in an embodiment of the present utility model;

[0022] Figure 2 A schematic diagram of the partial structure of a mixing element in a multi-stage enzymatic hydrolysis reaction device provided in an embodiment of the present utility model;

[0023] Figure 3 for Figure 2 Schematic diagram of the enlarged structure at Q in the middle;

[0024] Figure 4 A schematic diagram of the front structure of a mixing unit in a multi-stage enzymatic hydrolysis reaction device provided by an embodiment of the present utility model;

[0025] Figure 5 for Figure 4 a cross-sectional structure schematic view at A-A in the middle;

[0026] Figure 6 for Figure 5 an enlarged structure schematic view at W in the middle;

[0027] Figure 7 a partial structure schematic view of the fine heating element in the multi-section enzymolysis reaction device provided by the embodiment of the utility model;

[0028] Figure 8 a front structure schematic view of the fine heating element in the multi-section enzymolysis reaction device provided by the embodiment of the utility model;

[0029] Figure 9 for Figure 8 a cross-sectional structure schematic view at B-B in the middle;

[0030] Figure 10 for Figure 9 an enlarged structure schematic view at E in the middle;

[0031] Figure 11 a cross-sectional structure schematic view of the filter in the multi-section enzymolysis reaction device provided by the embodiment of the utility model.

[0032] In the drawings, the component list represented by each sign is as follows:

[0033] 1, mixing tank body; 11, first chamber; 12, second chamber; 13, to be enzymolysis material feeding end; 14, acid and alkali liquid adding end; 15, pH detector; 16, liquid level sensor; 17, display;

[0034] 2, mixing element;

[0035] 21, stirring element; 211, stirring motor; 212, motor gear; 213, upper transmission gear; 214, transmission rod; 215, lower transmission gear; 216, stirring gear; 217, stirrer; 218, bearing element;

[0036] 22, initial heating element;

[0037] 23, fine heating element; 231, heating water tank; 232, support cylinder; 233, spiral pipe; 2331, spiral pipe pump; 234, outer ring heating jacket; 2341, outer inlet and outlet water pipe; 2342, outer water pump; 235, inner ring heating jacket; 2351, inner inlet and outlet water pipe; 2352, inner water pump; 236, outer temperature sensor; 237, inner temperature sensor;

[0038] 3, collecting element; 31, collecting tank; 32, filter; 33, valve body. DETAILED DESCRIPTION

[0039] To facilitate understanding of the present application, the present application will be described more fully below with reference to the accompanying drawings. The accompanying drawings provide embodiments of the present application. However, the present application may be implemented in many different forms and is not limited to the embodiments described herein. Rather, these embodiments are provided to make the disclosure of the present application more thorough and comprehensive.

[0040] Unless otherwise defined, all technical and scientific terms used herein have the same meaning as those commonly understood by those skilled in the art to which this application pertains. The terms used herein in the specification of this application are for the purpose of describing specific embodiments only and are not intended to limit this application.

[0041] It will be understood that spatial relational terms such as "under," "beneath," "below," "under," "above," "above," etc., may be used herein to describe the relationship of an element or feature shown in the figures to other elements or features. It will be understood that in addition to the orientations shown in the figures, spatial relational terms also include different orientations of the device in use and operation. For example, if the device in the drawings is turned over, the element or feature described as "under" or "beneath" or "beneath" the other elements will be oriented as "above" the other elements or features. Thus, the exemplary terms "under" and "under" may include both upper and lower orientations. In addition, the device may also include alternative orientations (e.g., rotated 90 degrees or other orientations), and the spatial descriptors used herein are interpreted accordingly.

[0042] It should be noted that when an element is considered to be "connected" to another element, it can be directly connected to the other element or connected to the other element through an intermediate element. In the following embodiments, "connection" should be understood as "electrical connection", "communication connection", etc., if the connected circuits, modules, units, etc. can transmit electrical signals or data to each other.

[0043] When used herein, the singular forms "a", "an", and "the" may also include the plural forms, unless the context clearly indicates otherwise. It should also be understood that the terms "include / comprise" or "have" and the like specify the presence of stated features, integers, steps, operations, components, parts, or combinations thereof, but do not preclude the possibility of the presence or addition of one or more other features, integers, steps, operations, components, parts, or combinations thereof.

[0044] like Figures 1 to 11As shown, a multi-stage enzymatic hydrolysis reaction device includes a mixing tank body 1, a mixing element 2 and a collecting element 3, wherein the mixing tank body 1 is provided with a first chamber 11 and a second chamber 12; the mixing element 2 includes a stirring element 21, a primary heating element 22 and a fine heating element 23, the stirring element 21 is rotatably connected to the first chamber 11, and can stir the material to be enzymatically hydrolyzed in the first chamber 11 evenly; the primary heating element 22 is provided in the second chamber 12, and can heat the first chamber 11; the fine heating element 23 is connected to the first chamber 11, and can temperature-control and heat the material to be enzymatically hydrolyzed that is evenly mixed in the first chamber 11; the collecting element 3 is connected to the fine heating element 23, and can collect the enzymatic hydrolysis material.

[0045] In this embodiment, the stirring member 21 and the primary heating member 22 of the mixing member 2 are arranged in the first chamber 11 of the mixing tank body 1. While the stirring member 21 stirs the material to be hydrolyzed evenly, the primary heating member 22 preliminarily heats the material to be hydrolyzed to fully mix the material to be hydrolyzed. After sufficient mixing, the fine heating member 23 is used to make the material to be hydrolyzed reach the optimal hydrolysis temperature, thereby achieving the best hydrolysis effect. Thus, the problem of poor control of the hydrolysis temperature in the prior art is solved.

[0046] In some embodiments, the stirring member 21 includes a stirring motor 211, a motor gear 212, an upper transmission gear 213, a transmission rod 214, a lower transmission gear 215, a stirring gear 216 and an agitator 217. The stirring motor 211 is provided with a fixed end and a rotating end. The fixed end of the stirring motor 211 is connected to the mixing tank body 1; the motor gear 212 is connected to the rotating end of the stirring motor 211; the upper transmission gear 213 is meshed with the motor gear 212; the transmission rod 214 is penetrated by the mixing tank body 1, the upper end of the transmission rod 214 is connected to the upper transmission gear 213, and the middle part of the transmission rod 214 is rotatably connected to the mixing tank body 1; the lower transmission gear 215 is connected to the lower end of the transmission rod 214; the stirring gear 216 is rotatably connected to the mixing tank body 1, and the stirring gear 216 is meshed with the lower transmission gear 215; the agitator 217 is connected to the stirring gear 216.

[0047] In this embodiment, the stirring motor 211 drives the motor gear 212 to rotate, the motor gear 212 drives the upper transmission gear 213 to rotate, the upper transmission gear 213 drives the transmission rod 214 to rotate, the transmission rod 214 drives the lower transmission gear 215 to rotate, and the lower transmission gear 215 drives the stirring gear 216 to rotate. The stirrer 217 is fixed to the stirring gear 216 and, driven by the stirring gear 216, the stirrer 217 fully stirs the material to be enzymatically hydrolyzed. In addition, the stirring motor 211 is a servo motor.

[0048] In some embodiments, a bearing member 218 is further included, wherein the outer ring of the bearing member 218 is connected to the mixing tank body 1 , and the inner ring of the bearing member 218 is connected to the transmission rod 214 .

[0049] In this embodiment, the outer ring of the bearing member 218 is connected to the mixing tank body 1, and the inner ring of the bearing member 218 is connected to the transmission rod 214. Thus, the transmission rod 214 is better connected to the mixing tank body 1.

[0050] In some embodiments, the fine heating element 23 includes a heating water tank 231, a support cylinder 232, a spiral tube 233, a spiral tube pump 2331, an outer ring heating jacket 234, an outer inlet and outlet water pipe 2341, an outer water pump 2342, an inner ring heating jacket 235, an inner inlet and outlet water pipe 2351 and an inner water pump 2352, the support cylinder 232 is connected to one side of the heating water tank 231; the spiral tube 233 is connected to the support cylinder 232, and the feed end of the spiral tube 233 is connected to the mixing tank body 1; the spiral tube pump 2331 is connected to one side of the spiral tube 233, and can pump the material to be enzymatically hydrolyzed in the mixing tank body 1 into the spiral tube 233; one side of the outer ring heating jacket 234 is connected to the support cylinder 232, and the other side of the outer ring heating jacket 234 is connected to the spiral tube 2 33 connection; the middle part of the outer inlet and outlet water pipe 2341 is connected to the outer ring heating jacket 234, and the two ends of the outer inlet and outlet water pipe 2341 are connected to the heating water tank 231; the outer water pump 2342 is connected to the outer inlet and outlet water pipe 2341, and can pump the water of the heating water tank 231 into the outer ring heating jacket 234; the inner ring heating jacket 235 is connected to the inner ring of the spiral tube 233, and the two ends of the inner ring heating jacket 235 are connected to the heating water tank 231; the middle part of the inner inlet and outlet water pipe 2351 is connected to the inner ring heating jacket 235, and the two ends of the inner inlet and outlet water pipe 2351 are connected to the heating water tank 231; the inner water pump 2352 is connected to the inner inlet and outlet water pipe 2351, and can pump the water of the heating water tank 231 into the inner ring heating jacket 235.

[0051] In this embodiment, the external water pump 2342 transports the hot water heated to a certain temperature in the heating water tank 231 to the outer outer ring heating sleeve 234. The internal water pump 2352 transports the hot water heated to a certain temperature in the heating water tank 231 to the inner ring heating sleeve 235. The spiral tube pump 2331 transports the material to be enzymolyzed in the mixing tank body 1 to the spiral tube 233. Thus, the material to be enzymolyzed in the spiral tube 233 is fully enzymolyzed. Secondly, the length of the spiral tube 233 is lengthened or shortened according to actual needs to increase the enzymolysis effect, which should fall within the scope of protection of this application. In addition, a heating element is provided in the heating water tank 231, and the heating element belongs to conventional technical means in this field and will not be described here one by one.

[0052] In some embodiments, an external temperature sensor 236 and an internal temperature sensor 237 are further included. The external temperature sensor 236 is connected to the outside of the spiral tube 233 ; the internal temperature sensor 237 is connected to the inside of the spiral tube 233 .

[0053] In this embodiment, an external temperature sensor 236 is connected to the outside of the spiral tube 233, while an internal temperature sensor 237 is connected to the inside of the spiral tube 233. To improve temperature control accuracy during the heating process of the precision heating element 23, sensing devices are installed on both the inside and outside of the spiral tube 233 to ensure optimal enzymatic hydrolysis temperature. Furthermore, both the external temperature sensor 236 and the internal temperature sensor 237 utilize the MLX90614 infrared temperature sensor.

[0054] In some embodiments, the collecting member 3 includes a collecting tank 31 , at least one collecting tank 31 is provided, and the collecting tank 31 is connected to the discharge end of the spiral tube 233 .

[0055] In some embodiments, the collecting member 3 further includes a filter 32 and a valve body 33, the filter 32 is connected to the feed end of the collecting tank 31; the inlet end of the valve body 33 is connected to the discharge end of the spiral tube 233, and the outlet end of the valve body 33 is connected to the filter 32.

[0056] In this embodiment, when the valve body 33 is a two-way valve, the inlet of the two-way valve is connected to the spiral tube 233, the outlet end of the two-way valve is connected to the collection tank 31, and the filter 32 between the valve body 33 and the collection tank 31 is used to filter impurities. When the valve body 33 is a three-way valve, the inlet of the three-way valve is connected to the spiral tube 233, the two outlet ends of the three-way valve are connected to the collection tank 31, and the filter 32 between the valve body 33 and the collection tank 31 is used to filter impurities. When there are too many impurities in the filter 32 and it needs to be replaced, it is only necessary to control the three-way valve at the connection end to close and replace it. When the valve body 33 is a three-way valve, its principle is similar to the above principle and will not be described in detail here.

[0057] In some embodiments, the mixing tank body 1 is connected to a feed end 13 of a material to be enzymatically hydrolyzed and an acid and alkali solution addition end 14 .

[0058] In some embodiments, a pH value detector 15 and a liquid level sensor 16 are provided in the mixing tank 1 .

[0059] In some embodiments, a display 17 is provided on the mixing tank body 1 , and the display 17 is electrically connected to the pH value detector 15 and the liquid level sensor 16 , and can display the liquid level and pH value of the material to be enzymatically hydrolyzed in the mixing tank body 1 .

[0060] In the present embodiment, when the liquid level sensor 16 senses that the enzymolysis material is reduced, the enzymolysis material feed end 13 is used to increase the enzymolysis material in the mixing tank body 1. When the pH value detector 15 detects that the pH value has not reached the optimal enzymolysis effect, the pH regulating liquid is added through the acid and alkali solution adding end 14 to adjust the pH value. Secondly, the display 17 can display the liquid level height and pH value of the material to be enzymolyzed in the mixing tank body 1 to facilitate the operator's operation. In addition, the pH value detector 15 adopts an industrial online pH meter controller. The liquid level sensor 16 adopts an XKCY2824V liquid level gauge sensor.

[0061] Compared with the prior art, the technical solution of this application has the following beneficial technical effects:

[0062] The stirring element and the primary heating element of the mixing unit are disposed within the first chamber of the mixing tank. While the stirring element uniformly stirs the material to be hydrolyzed, the primary heating element preliminarily heats the material to be hydrolyzed, ensuring thorough mixing. After thorough mixing, the final heating element brings the material to the optimal hydrolysis temperature, thereby achieving the best hydrolysis effect. This solves the problem of poor hydrolysis temperature control in the prior art, which results in poor hydrolysis results.

[0063] The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention should be included in the scope of protection of the present invention.

Claims

1. A multi-stage enzymatic hydrolysis reaction device, characterized in that: include: A mixing tank (1) is provided with a first chamber (11) and a second chamber (12); A mixing element (2), comprising: a stirring member (21) rotatably connected to the first chamber (11) and capable of uniformly stirring the material to be enzymatically hydrolyzed in the first chamber (11); a primary heating element (22), which is disposed in the second chamber (12) and is capable of heating the first chamber (11); a fine heating element (23), which is connected to the first chamber (11) and can heat the uniformly mixed material to be enzymatically hydrolyzed in the first chamber (11) at a controlled temperature; The collecting element (3) is connected to the fine heating element (23) and can collect the enzymatically hydrolyzed material.

2. A multi-stage enzymatic hydrolysis reaction device according to claim 1, characterized in that: The stirring member (21) comprises: A stirring motor (211) is provided with a fixed end and a rotating end, wherein the fixed end of the stirring motor (211) is connected to the mixing tank body (1); a motor gear (212) connected to the rotating end of the stirring motor (211); an upper transmission gear (213) meshing with the motor gear (212); A transmission rod (214) is provided through the mixing tank body (1), the upper end of the transmission rod (214) is connected to the upper transmission gear (213), and the middle portion of the transmission rod (214) is rotationally connected to the mixing tank body (1); a lower transmission gear (215) connected to the lower end of the transmission rod (214); a stirring gear (216) which is rotatably connected to the mixing tank body (1), and the stirring gear (216) is meshed with the lower transmission gear (215); A stirrer (217) is connected to the stirring gear (216).

3. A multi-stage enzymatic hydrolysis reaction device according to claim 2, characterized in that: Also includes: The outer ring of the bearing member (218) is connected to the mixing tank body (1), and the inner ring of the bearing member (218) is connected to the transmission rod (214).

4. A multi-stage enzymatic hydrolysis reaction device according to claim 1, characterized in that: The fine heating element (23) comprises: Heating water tank (231); A support cylinder (232) connected to one side of the heating water tank (231); A spiral tube (233) is connected to the support cylinder (232), and a feed end of the spiral tube (233) is connected to the mixing tank (1); A spiral tube pump (2331) is connected to one side of the spiral tube (233) and is capable of pumping the material to be enzymatically hydrolyzed in the mixing tank (1) into the spiral tube (233); An outer ring heating sleeve (234), one side of which is connected to the support cylinder (232), and the other side of which is connected to the spiral tube (233); An external water inlet and outlet pipe (2341), wherein the middle portion is connected to the outer ring heating jacket (234), and both ends of the external water inlet and outlet pipe (2341) are connected to the heating water tank (231); an external water pump (2342), connected to the external water inlet and outlet pipes (2341), capable of pumping water from the heating water tank (231) into the outer heating jacket (234); An inner ring heating jacket (235) is connected to the inner ring of the spiral tube (233), and both ends of the inner ring heating jacket (235) are in communication with the heating water tank (231); An inner water inlet and outlet pipe (2351), wherein the middle portion is connected to the inner ring heating jacket (235), and both ends of the inner water inlet and outlet pipe (2351) are connected to the heating water tank (231); The inner water pump (2352) is connected to the inner water inlet and outlet pipes (2351) and is capable of pumping water from the heating water tank (231) into the inner ring heating jacket (235).

5. A multi-stage enzymatic hydrolysis reaction device according to claim 4, characterized in that: Also includes: an external temperature sensor (236) connected to the outside of the spiral tube (233); An internal temperature sensor (237) is connected to the inner side of the spiral tube (233).

6. A multi-stage enzymatic hydrolysis reaction device according to claim 4, characterized in that: The collecting member (3) comprises: A collecting tank (31) is provided, wherein at least one collecting tank (31) is connected to the discharge end of the spiral tube (233).

7. A multi-stage enzymatic hydrolysis reaction device according to claim 6, characterized in that: The collecting member (3) further comprises: a filter (32) connected to the feed end of the collection tank (31); The inlet end of the valve body (33) is connected to the discharge end of the spiral tube (233), and the outlet end of the valve body (33) is connected to the filter (32).

8. A multi-stage enzymatic hydrolysis reaction device according to claim 1, characterized in that: The mixing tank body (1) is connected to a feed end (13) for the material to be enzymatically hydrolyzed and an acid and alkali solution addition end (14).

9. A multi-stage enzymatic hydrolysis reaction device according to claim 1, characterized in that: A pH value detector (15) and a liquid level sensor (16) are provided in the mixing tank (1).

10. A multi-stage enzymatic hydrolysis reaction device according to claim 9, characterized in that: The mixing tank body (1) is provided with a display (17), and the display (17) is electrically connected to the pH value detector (15) and the liquid level sensor (16), and can display the liquid level height and pH value of the material to be enzymatically hydrolyzed in the mixing tank body (1).

Citation Information

Patent Citations

  • Enzymolysis reaction kettle

    CN107974404A