CN114672414A - Constant temperature enzymolysis retort - Google Patents

Constant temperature enzymolysis retort Download PDF

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Publication number
CN114672414A
CN114672414A CN202210596689.3A CN202210596689A CN114672414A CN 114672414 A CN114672414 A CN 114672414A CN 202210596689 A CN202210596689 A CN 202210596689A CN 114672414 A CN114672414 A CN 114672414A
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CN
China
Prior art keywords
enzymolysis
box
constant
suspension
ring
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Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN202210596689.3A
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Chinese (zh)
Inventor
冯二豪
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Shenzhen Luyang Agricultural Technology Co ltd
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Shenzhen Luyang Agricultural Technology Co ltd
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Priority to CN202210596689.3A priority Critical patent/CN114672414A/en
Publication of CN114672414A publication Critical patent/CN114672414A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M21/00Bioreactors or fermenters specially adapted for specific uses
    • C12M21/18Apparatus specially designed for the use of free, immobilized or carrier-bound enzymes
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M23/00Constructional details, e.g. recesses, hinges
    • C12M23/38Caps; Covers; Plugs; Pouring means
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M23/00Constructional details, e.g. recesses, hinges
    • C12M23/56Floating elements
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M27/00Means for mixing, agitating or circulating fluids in the vessel
    • C12M27/02Stirrer or mobile mixing elements
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M41/00Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/12Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
    • C12M41/18Heat exchange systems, e.g. heat jackets or outer envelopes
    • C12M41/22Heat exchange systems, e.g. heat jackets or outer envelopes in contact with the bioreactor walls

Abstract

The invention is suitable for a biological treatment device, and particularly relates to a constant-temperature enzymolysis reaction tank, which comprises: the heating box is internally sleeved with a suspension box, the suspension box is fixedly connected with the heating box, and an enzymolysis box is arranged in the suspension box; the circulating water bath mechanism is arranged between the heating box and the suspension box and is used for driving constant-temperature water flow to flow in the heating box and the suspension box; stirring enzymolysis mechanism, stirring enzymolysis mechanism fixed mounting is in the enzymolysis tank for stir the enzymolysis fluid. According to the invention, the enzymolysis tank is arranged, substances to be subjected to enzymolysis are put into the enzymolysis tank, the raw materials are stirred by the stirring enzymolysis mechanism in the enzymolysis process, the raw material mixing is promoted, the heat exchange is improved, the temperature uniformity is improved, the medium is continuously heated by the circulating water bath mechanism, the flowing medium is continuously contacted with the enzymolysis tank, the constant enzymolysis temperature is ensured, and the enzymolysis efficiency is improved.

Description

Constant temperature enzymolysis retort
Technical Field
The invention belongs to a biological treatment device, and particularly relates to a constant-temperature enzymolysis reaction tank.
Background
The biological enzymolysis technology is applied to human health, agriculture, industry and environment, and has some applications in other fields, and the application range is wide. Most of the applications in the field of human health have succeeded in creating productivity for human health engineering. The basic subject of the biological enzymolysis technology is that the substances are fully decomposed under the action of enzyme to obtain the extract required by the biological engineering.
The biological enzymolysis technology has the advantages that substances are decomposed by self under the catalysis of enzyme, and the capability of enzyme catalyzing chemical reaction is called enzyme activity (or enzyme activity). The enzyme activity can be regulated and controlled by various factors, so that the organism can adapt to the change of external conditions and maintain the life activity. By utilizing different catalytic actions of different enzymes, the characteristics of different active ingredients of the substance can be grasped, and the active substances of the substance can be extracted.
In the prior art, the enzymolysis reaction tank is simple in structure, and the sufficient mixing of substances in the enzymolysis process cannot be guaranteed, so that the enzymolysis efficiency is low.
Disclosure of Invention
The embodiment of the invention aims to provide a constant-temperature enzymolysis reaction tank, and aims to solve the problems in the third part of the background art.
The embodiment of the invention is realized in such a way that the constant-temperature enzymolysis reaction tank comprises:
the heating box is internally sleeved with a suspension box, the suspension box is fixedly connected with the heating box, and an enzymolysis box is arranged in the suspension box;
the circulating water bath mechanism is arranged between the heating box and the suspension box and is used for driving constant-temperature water flow to flow in the heating box and the suspension box;
stirring enzymolysis mechanism, stirring enzymolysis mechanism fixed mounting is in the enzymolysis tank for stir the enzymolysis fluid.
Preferably, the stirring enzymolysis mechanism comprises:
the mixed flow structure is slidably arranged in the enzymolysis box and is used for stirring the enzymolysis fluid;
and the adjusting structure is fixedly arranged in the mixed flow structure and is used for adjusting the stirring direction of the mixed flow structure.
Preferably, the mixed flow structure is including sealed lid, be provided with elastic sealing ring on the sealed external diameter of covering, be provided with the installation cavity in the sealed lid, install the motor in the installation cavity, be connected with the worm on the motor, the worm wheel is installed to the installation cavity internal rotation, worm wheel and worm meshing, fixedly connected with owner auger on the worm wheel, fixedly connected with multiunit telescopic cylinder on the main auger external diameter, it is provided with the telescopic link to slide in the telescopic cylinder, through spring coupling between telescopic link and the telescopic cylinder, the telescopic link tip rotates and is connected with the gear, the supplementary auger of fixedly connected with on the gear, supplementary auger is the same with the blade of owner auger to revolve to, the fixed outer ring gear that is provided with in sealed lid bottom, outer ring gear is used for with gear engagement.
Preferably, adjust the structure and include the cable, the fixed first coil that is provided with in installation cavity top, the fixed adjusting box that is provided with in main auger top, the fixed second coil that is provided with in adjusting box inner chamber top, still fixed mounting has electric putter in the adjusting box, all be provided with the spacing ring on telescopic link and the telescopic cylinder, spacing ring and telescopic link fixed connection are passed through to cable one end, and the other end gets into main auger inner chamber through the through-hole that sets up on main auger external diameter, and with electric putter fixed connection, sealed bottom of covering is provided with interior ring gear, interior ring gear is located outer ring gear inboard, the gear is located between interior ring gear and the outer ring gear.
Preferably, circulation water bath mechanism includes heater strip and water pump, and water pump fixed mounting is in heating cabinet inner chamber bottom, through water ring fixed connection of intaking between heating cabinet bottom and the suspension bottom of the case portion, and the water pump is located into water ring inboard, is provided with the inlet opening on the water ring of intaking, is provided with the heater strip between suspension outer wall and the heating cabinet inner wall, is provided with the backward flow mouth on the suspension case.
Preferably, the inlet opening is provided with the multiunit, and along the water ring external diameter evenly distributed of intaking.
Preferably, the outer diameter of the enzymolysis tank is fixed with a buoyancy ring, and the inner wall of the suspension tank is fixedly provided with a limiting plate.
The constant-temperature enzymolysis reaction tank provided by the embodiment of the invention has the advantages that the structure is simple, the design is reasonable, substances needing enzymolysis are put into the tank through the enzymolysis box, the raw materials are stirred by the stirring enzymolysis mechanism in the enzymolysis process, the raw material mixing is promoted, the heat exchange is improved, the temperature uniformity is improved, the medium is continuously heated by the circulating water bath mechanism, the flowing medium is continuously contacted with the enzymolysis box, the constant enzymolysis temperature is ensured, and the enzymolysis efficiency is improved.
Drawings
FIG. 1 is a schematic structural diagram of a constant-temperature enzymolysis reaction tank provided in an embodiment of the present invention;
FIG. 2 is an enlarged view of a portion of FIG. 1 at A;
FIG. 3 is a schematic view of a portion of a flow mixing structure according to an embodiment of the present invention;
fig. 4 is a schematic structural diagram of a sealing cover according to an embodiment of the present invention.
In the drawings: 1. a heating box; 2. a suspension tank; 3. heating wires; 4. a return port; 5. a limiting plate; 6. a buoyancy ring; 7. an enzymolysis box; 8. a sealing cover; 9. an elastic sealing ring; 10. a motor; 11. a mounting cavity; 12. a worm; 13. a telescopic cylinder; 14. a telescopic rod; 15. an inner gear ring; 16. an outer ring gear; 17. an auxiliary auger; 18. a main auger; 19. a spring; 20. a water pump; 21. a water inlet ring; 22. a water inlet hole; 23. a first coil; 24. an adjustment box; 25. a second coil; 26. an electric push rod; 27. a worm gear; 28. a gear; 29. a limiting ring; 30. a cable; 100. a stirring enzymolysis mechanism; 101. a mixed flow structure; 102. an adjustment structure; 200. circulating water bath mechanism.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more apparent, the present invention is described in further detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
Specific implementations of the present invention are described in detail below with reference to specific embodiments.
As shown in fig. 1, which is a schematic structural diagram of a constant-temperature enzymolysis reaction tank provided in an embodiment of the present invention, the constant-temperature enzymolysis reaction tank includes:
the device comprises a heating box 1, wherein a suspension box 2 is sleeved in the heating box 1, the suspension box 2 is fixedly connected with the heating box 1, and an enzymolysis box 7 is arranged in the suspension box 2;
the circulating water bath mechanism 200 is arranged between the heating box 1 and the suspension box 2 and is used for driving constant-temperature water flow to flow in the heating box 1 and the suspension box 2;
stirring enzymolysis mechanism 100, stirring enzymolysis mechanism 100 fixed mounting is in enzymolysis tank 7 for stir the enzymolysis fluid.
In this embodiment, during the use, the raw materials that will need enzymolysis drop into enzymolysis tank 7 in, and utilize stirring enzymolysis mechanism 100 to seal it, when the enzymolysis, utilize circulation water bath mechanism 200 constantly to produce the medium of appointed temperature, the medium is heated in heating cabinet 1, flow through suspension case 2 afterwards, enzymolysis tank 7 suspends in suspension case 2, its week directly contacts with the medium, and carry out the heat exchange with the medium, at this in-process, through setting up the temperature sensor in enzymolysis tank 7, measure the temperature everywhere in enzymolysis tank 7, thereby confirm its temperature distribution condition, and then adjust the stirring direction according to temperature distribution.
As shown in fig. 1, as a preferred embodiment of the present invention, the stirring enzymolysis mechanism 100 includes:
the mixed flow structure 101 is slidably mounted in the enzymolysis tank 7, and is used for stirring enzymolysis fluid;
and the adjusting structure 102 is fixedly installed in the mixed flow structure 101, and is used for adjusting the stirring direction of the mixed flow structure 101.
In the embodiment, when mixing, the raw materials added into the enzymolysis tank 7 are stirred and mixed by the mixed flow structure 101, the temperature of each part of the raw materials is monitored to determine the temperature level of each part, so as to generate an adjusting scheme, and the rotation direction and the stirring direction of the mixed flow structure 101 are controlled by the adjusting structure 102.
As shown in fig. 1, 3 and 4, as a preferred embodiment of the present invention, the flow mixing structure 101 includes a sealing cover 8, be provided with elastic sealing ring 9 on the 8 external diameters of sealed lid, be provided with installation cavity 11 in the sealed lid 8, install motor 10 in the installation cavity 11, be connected with worm 12 on the motor 10, worm wheel 27 is installed to 11 internal rotations in installation cavity, worm wheel 27 and worm 12 meshing, worm wheel 27 goes up main auger 18 of fixedly connected with, fixedly connected with multiunit telescopic cylinder 13 on the 18 external diameters of main auger, it is provided with telescopic link 14 to slide in telescopic cylinder 13, be connected through spring 19 between telescopic link 14 and the telescopic cylinder 13, 14 tip rotations of telescopic link are connected with gear 28, the last supplementary auger 17 of fixedly connected with of gear 28, supplementary auger 17 is the same with the blade of main auger 18 soon, the fixed outer ring gear 16 that is provided with in sealed lid 8 bottom, outer ring gear 16 is used for meshing with gear 28.
As shown in fig. 1, 2 and 4, as a preferred embodiment of the present invention, the adjusting structure 102 includes a pulling cable 30, a first coil 23 is fixedly disposed on the top of the mounting cavity 11, an adjusting box 24 is fixedly disposed on the top of the main packing auger 18, a second coil 25 is fixedly disposed on the top of an inner cavity of the adjusting box 24, an electric push rod 26 is further fixedly disposed in the adjusting box 24, both the telescopic rod 14 and the telescopic cylinder 13 are provided with a limit ring 29, one end of the pulling cable 30 is fixedly connected to the telescopic rod 14 through the limit ring 29, and the other end of the pulling cable enters the inner cavity of the main packing auger 18 through a through hole disposed on the outer diameter of the main packing auger 18 and is fixedly connected to the electric push rod 26, an inner toothed ring 15 is disposed at the bottom of the sealing cover 8, the inner toothed ring 15 is disposed on the inner side of the outer toothed ring 16, and the gear 28 is disposed between the inner toothed ring 15 and the outer toothed ring 16.
In this embodiment, a temperature sensor is arranged in the enzymolysis tank 7, the temperature of the bottom, the top and the outer diameter of the enzymolysis tank 7 is respectively detected, when stirring, the motor 10 is started, the motor 10 drives the worm 12 to rotate, the worm 12 drives the main screw 18 to rotate through the worm wheel 27, the main screw 18 drives the auxiliary screw 17 to rotate, during the rotation, the gear 28 is meshed with the inner toothed ring 15 or the outer toothed ring 16, so that the auxiliary screw 17 and the main screw 18 keep the same or opposite rotation direction, the meshing of the gear 28 and the inner toothed ring 15 or the outer toothed ring 16 is controlled through the adjusting structure 102, in the initial state, the spring 19 drives the expansion rod 14 to extend relative to the expansion cylinder 13 until the gear 28 at the end of the expansion rod 14 is meshed with the outer toothed ring 16, at this time, the rotation direction of the auxiliary screw 17 is opposite to that of the main screw 18, so that when the main screw 18 stirs the raw materials upwards, the auxiliary auger 17 downwards stirs the raw materials, the raw materials positioned in the core part of the enzymolysis tank 7 are upwards transported at the moment, the raw materials move towards two sides after reaching the top part, the raw materials are downwards transported along the edge of the enzymolysis tank 7 and then return to the core part to realize the forward movement of the internal raw materials, the circulation mode is used for keeping the bottom temperature in the enzymolysis tank 7 low and the top temperature high, when the bottom temperature in the enzymolysis tank 7 is high and the top temperature is low, the rotation directions of the auxiliary auger 17 and the main auger 18 are opposite, and the motor 10 is enabled to be reverse; the first coil 23 supplies power to the second coil 25, the second coil 25 supplies power to the electric push rod 26, the electric push rod 26 drives the telescopic rod 14 to gradually enter the telescopic cylinder 13 through the guy cable 30 until the gear 28 is meshed with the inner gear ring 15, at the moment, the rotation directions of the auxiliary auger 17 and the main auger 18 are the same, the auxiliary auger 17 and the main auger 18 can be controlled to rotate forwards or reversely simultaneously by changing the rotation direction of the motor, the sealing cover 8 is provided with an air pressure balance hole, the auxiliary auger 17 and the main auger 18 rotate forwards simultaneously when the sealing cover 8 is installed, the enzymolysis raw materials are stirred upwards, the auxiliary auger 17 and the main auger 18 can pull the sealing cover 8 downwards under the driving of the reaction force, the sealing cover 8 slides downwards gradually, and when the enzymolysis is finished, the rotation direction of the motor is changed to control the auxiliary auger 17 and the main auger 18 to rotate backwards simultaneously, at this time, the enzymolysis raw material is stirred downwards, and the sealing cover 8 slides upwards relative to the enzymolysis box 7.
As shown in fig. 1, as a preferred embodiment of the present invention, the circulating water bath mechanism 200 includes a heating wire 3 and a water pump 20, the water pump 20 is fixedly installed at the bottom of the inner cavity of the heating box 1, the bottom of the heating box 1 is fixedly connected with the bottom of the suspension box 2 through a water inlet ring 21, the water pump 20 is located inside the water inlet ring 21, the water inlet ring 21 is provided with a water inlet 22, the heating wire 3 is arranged between the outer wall of the suspension box 2 and the inner wall of the heating box 1, and the suspension box 2 is provided with a return opening 4.
In this embodiment, heat the medium through heater strip 3, the medium after the heating enters into water ring 21 inboard through inlet opening 22 to inhale through water pump 20, utilize water pump 20 to carry the medium to suspension case 2 bottom, the liquid level in suspension case 2 rises gradually, and at this in-process, the medium directly carries out the heat exchange with suspension case 2, and the medium in suspension case 2 finally gets back to in the heating cabinet 1 through backward flow mouth 4.
As shown in fig. 1, as a preferred embodiment of the present invention, the water inlet holes 22 are provided in a plurality of groups and uniformly distributed along the outer diameter of the water inlet ring 21.
As shown in FIG. 1, as a preferred embodiment of the present invention, a buoyancy ring 6 is fixed on the outer diameter of the enzymolysis tank 7, and a limit plate 5 is fixed on the inner wall of the suspension tank 2.
In this embodiment, can guarantee through setting up buoyancy ring 6 that enzymolysis tank 7 can suspend in the middle of suspension case 2, set up limiting plate 5 and be used for avoiding enzymolysis tank 7 come-up under the impact of medium.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents and improvements made within the spirit and principle of the present invention are intended to be included within the scope of the present invention.

Claims (7)

1. The utility model provides a constant temperature enzymolysis retort which characterized in that, constant temperature enzymolysis retort includes:
the heating box is internally sleeved with a suspension box, the suspension box is fixedly connected with the heating box, and an enzymolysis box is arranged in the suspension box;
the circulating water bath mechanism is arranged between the heating box and the suspension box and is used for driving constant-temperature water flow to flow in the heating box and the suspension box;
stirring enzymolysis mechanism, stirring enzymolysis mechanism fixed mounting is in the enzymolysis tank for stir the enzymolysis fluid.
2. The constant-temperature enzymolysis reaction tank of claim 1, wherein the stirring enzymolysis mechanism comprises:
the mixed flow structure is slidably arranged in the enzymolysis box and is used for stirring enzymolysis fluid;
and the adjusting structure is fixedly arranged in the mixed flow structure and is used for adjusting the stirring direction of the mixed flow structure.
3. The constant-temperature enzymolysis reaction tank as claimed in claim 2, wherein the mixed flow structure comprises a sealing cover, an elastic sealing ring is arranged on the outer diameter of the sealing cover, an installation cavity is arranged in the sealing cover, a motor is installed in the installation cavity, a worm is connected to the motor, a worm wheel is installed in the installation cavity in a rotating mode, the worm wheel is meshed with the worm, a main auger is fixedly connected to the worm wheel, a plurality of groups of telescopic cylinders are fixedly connected to the outer diameter of the main auger, telescopic rods are arranged in the telescopic cylinders in a sliding mode, the telescopic rods are connected with the telescopic cylinders through springs, gears are rotatably connected to the end portions of the telescopic rods, auxiliary augers are fixedly connected to the gears, the auxiliary augers are identical to the rotating direction of blades of the main auger, outer toothed rings are fixedly arranged at the bottom of the sealing cover, and are used for being meshed with the gears.
4. The constant-temperature enzymolysis reaction tank as claimed in claim 3, wherein the adjusting structure comprises a stay cable, a first coil is fixedly arranged at the top of the installation cavity, an adjusting box is fixedly arranged at the top of the main auger, a second coil is fixedly arranged at the top of the inner cavity of the adjusting box, an electric push rod is further fixedly arranged in the adjusting box, limit rings are arranged on the telescopic rod and the telescopic cylinder, one end of the stay cable is fixedly connected with the telescopic rod through the limit ring, the other end of the stay cable enters the inner cavity of the main auger through a through hole formed in the outer diameter of the main auger and is fixedly connected with the electric push rod, an inner toothed ring is arranged at the bottom of the sealing cover, the inner toothed ring is positioned inside the outer toothed ring, and the gear is positioned between the inner toothed ring and the outer toothed ring.
5. The constant-temperature enzymolysis reaction tank of claim 1, wherein the circulating water bath mechanism comprises a heating wire and a water pump, the water pump is fixedly installed at the bottom of the inner cavity of the heating box, the bottom of the heating box and the bottom of the suspension box are fixedly connected through a water inlet ring, the water pump is located on the inner side of the water inlet ring, a water inlet hole is formed in the water inlet ring, the heating wire is arranged between the outer wall of the suspension box and the inner wall of the heating box, and a backflow port is formed in the suspension box.
6. The constant-temperature enzymolysis reaction tank of claim 5, wherein the water inlet holes are provided with a plurality of groups and are uniformly distributed along the outer diameter of the water inlet ring.
7. The constant-temperature enzymolysis reaction tank of claim 1, wherein a buoyancy ring is fixed on the outer diameter of the enzymolysis tank, and a limiting plate is fixed on the inner wall of the suspension tank.
CN202210596689.3A 2022-05-30 2022-05-30 Constant temperature enzymolysis retort Pending CN114672414A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202210596689.3A CN114672414A (en) 2022-05-30 2022-05-30 Constant temperature enzymolysis retort

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Application Number Priority Date Filing Date Title
CN202210596689.3A CN114672414A (en) 2022-05-30 2022-05-30 Constant temperature enzymolysis retort

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116555023A (en) * 2023-05-31 2023-08-08 青岛浩大生物科技工程有限责任公司 Corrosion-resistant fishskin and fish scale enzymolysis device

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008237213A (en) * 2007-02-26 2008-10-09 Toray Ind Inc Continuous fermentation apparatus
US20130217074A1 (en) * 2010-06-17 2013-08-22 Borregaard As Enzymatic Hydrolysis of Cellulose
CN106967601A (en) * 2017-05-18 2017-07-21 荣成市哥弟海洋生物科技有限公司 A kind of Fish protein extraction enzymolysis device
CN209128456U (en) * 2018-11-05 2019-07-19 天津赛尔康生物医药科技有限公司 A kind of enzymolysis device of giant salamander polypeptide powder
CN209940976U (en) * 2019-04-22 2020-01-14 山西吉呈生物技术有限公司 Stirring fermentation tank is used in pullulan production
CN211112034U (en) * 2019-10-24 2020-07-28 汕头市培芝食品有限公司 Be applied to enzymolysis device of rice
CN212713555U (en) * 2020-05-08 2021-03-16 常州市华人化工有限公司 Reaction unit is used in production of CBZ-L-valine
CN213726308U (en) * 2020-11-13 2021-07-20 江西省卓讯建材有限公司 High-efficient anti waterproofing agent dosing unit that splits

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008237213A (en) * 2007-02-26 2008-10-09 Toray Ind Inc Continuous fermentation apparatus
US20130217074A1 (en) * 2010-06-17 2013-08-22 Borregaard As Enzymatic Hydrolysis of Cellulose
CN106967601A (en) * 2017-05-18 2017-07-21 荣成市哥弟海洋生物科技有限公司 A kind of Fish protein extraction enzymolysis device
CN209128456U (en) * 2018-11-05 2019-07-19 天津赛尔康生物医药科技有限公司 A kind of enzymolysis device of giant salamander polypeptide powder
CN209940976U (en) * 2019-04-22 2020-01-14 山西吉呈生物技术有限公司 Stirring fermentation tank is used in pullulan production
CN211112034U (en) * 2019-10-24 2020-07-28 汕头市培芝食品有限公司 Be applied to enzymolysis device of rice
CN212713555U (en) * 2020-05-08 2021-03-16 常州市华人化工有限公司 Reaction unit is used in production of CBZ-L-valine
CN213726308U (en) * 2020-11-13 2021-07-20 江西省卓讯建材有限公司 High-efficient anti waterproofing agent dosing unit that splits

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
闻邦椿: "《机械设计手册机构设计》", 30 April 2020, 机械工业出版社 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116555023A (en) * 2023-05-31 2023-08-08 青岛浩大生物科技工程有限责任公司 Corrosion-resistant fishskin and fish scale enzymolysis device
CN116555023B (en) * 2023-05-31 2024-04-16 青岛浩大海洋生物科技股份有限公司 Corrosion-resistant fishskin and fish scale enzymolysis device

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