High-temperature and high-pressure enzymolysis tank for feather meal production

Abstract

The utility model discloses a high-temperature high-pressure enzymolysis tank for feather meal production, which belongs to the technical field of feather meal production and comprises an enzymolysis tank body, a variable-frequency gear motor is arranged at the top of the enzymolysis tank body, an output shaft of the variable-frequency gear motor is fixedly connected with a rotating shaft, and the bottom of the rotating shaft is fixedly connected with a stirring rod. Dissolved liquid is added into the enzymolysis tank body through the constant-temperature dropwise adding funnel, the variable-frequency gear motor is started, an output shaft of the variable-frequency gear motor rotates to enable the rotating shaft to rotate, the rotating shaft rotates to enable the stirring rod to rotate and enable raw materials to rotate, the constant-temperature oil bath pan is started, and water can enter the constant-temperature oil bath pan through the liquid conveying pipe via the inlet. After the interlayer is filled, the raw materials can be discharged and circulated through the outlet, and the raw materials can be subjected to high-temperature stirring, enzymolysis and hydrolysis at proper temperature in cooperation with detection of a glass thermometer, so that the effect of improving the digestibility of the feather meal can be achieved.

Description

Technical Field

[0001] The utility model belongs to the technical field of feather powder production, in particular to a high-temperature and high-pressure enzymolysis tank used for feather powder production. Background Art

[0002] Farmed poultry often encounter situations of self-pecking or mutual pecking, anus pecking, toe pecking, egg pecking and even feces pecking, which are collectively referred to as feather pecking or pecking addiction. Feather pecking not only seriously affects its value, but also causes complications of anemia, dermatitis, fragile and easy-to-break feathers, dull fur color, and sometimes causes the breeding of parasites. Therefore, feather pecking should be prevented and treated as early as possible. Hydrolyzed feather meal contains about 80% to 85% crude protein, and the content of sulfur-containing amino acids ranks first among all natural feeds. The content of valine, leucine and isoleucine ranks first, but the content of lysine and tryptophan is not high. Hydrolyzed feather meal has a good therapeutic effect on feather pecking. Feather pecking is rich in sulfur amino acids. Feeding in the spring and autumn molting season is beneficial to the growth and development of down. It also has the effect of reducing the anus pecking and hair jumping of chickens and ducks, and the self-biting and hair-eating phenomena of minks and foxes. In the production of feather meal, a high-temperature and high-pressure enzymatic hydrolysis tank for feather meal production is required.

[0003] In the prior art, a high-temperature and high-pressure enzymolysis tank used for feather meal production generally includes an enzymolysis tank body, the top of which is fixedly connected with an agitator, and water is introduced into the enzymolysis tank to stir the feather meal in the enzymolysis tank body through the agitator.

[0004] However, when the above device is used, it is difficult to control the temperature, resulting in a decrease in the digestibility of the feather meal. Utility Model Content

[0005] The purpose of the utility model is to solve the shortcomings of the prior art and to propose a high-temperature and high-pressure enzymolysis tank for feather powder production. The utility model has the advantages of improving the digestibility of feather powder.

[0006] In order to achieve the above purpose, the utility model adopts the following technical solutions:

[0007] A high-temperature and high-pressure enzymolysis tank for feather powder production comprises an enzymolysis tank body, a variable frequency reduction motor is arranged on the top of the enzymolysis tank body, an output shaft of the variable frequency reduction motor is fixedly connected to a rotating shaft, a stirring rod is fixedly connected to the bottom of the rotating shaft, the stirring rod is located in the enzymolysis tank body, an interlayer is provided on the wall surface of the enzymolysis tank body, an inlet is provided on the bottom of the outer wall on one side of the interlayer, an outlet is provided on the top of the outer wall on the other side of the interlayer, a constant temperature oil bath is arranged on one side of the enzymolysis tank body, and the constant temperature oil bath is fixedly connected to the inlet and the outlet respectively through infusion tubes.

[0008] Through the above technical scheme: when in use, the raw materials are added into the enzymolysis tank body, and then the dissolving liquid is added into the enzymolysis tank body through the constant temperature dropping funnel, the variable frequency reduction motor is started, the output shaft of the variable frequency reduction motor rotates to rotate the rotating shaft, the rotation of the rotating shaft can rotate the stirring rod, and the raw materials can be rotated, the constant temperature oil bath pot is started, the constant temperature oil bath pot can be filled with water through the inlet through the infusion tube, and after the interlayer is full, it can be discharged through the outlet and circulated, and the raw materials can be stirred at high temperature in conjunction with the detection of the glass thermometer, enzymolysis is carried out at 4000℃, and hydrolysis is carried out at 4000℃, thereby achieving the effect of improving the digestibility of feather meal.

[0009] The utility model is further configured that a base is provided at the bottom of the enzymolysis tank body, a connecting frame is fixedly connected to the top of the base, and the connecting frame is fixed to the variable frequency reduction motor and the enzymolysis tank body through a connecting piece.

[0010] Through the above technical solution: the setting of the base can make the stirring stable.

[0011] The utility model is further configured that the stirring rod is made of polytetrafluoroethylene.

[0012] Through the above technical solutions: it can be resistant to high temperature, corrosion, high lubricity, and non-adhesive to avoid interference with feather powder.

[0013] The utility model is further configured that a glass thermometer is fixedly connected to the top of the enzymatic hydrolysis tank, and a detection head of the glass thermometer is close to the feather powder.

[0014] Through the above technical solution: the setting of the glass thermometer can control the production temperature of feather meal.

[0015] The utility model is further configured that a digital display variable frequency speed regulator is fixedly connected to the top of the connecting frame, and the digital display variable frequency speed regulator is connected to the variable frequency reduction motor through an electric wire.

[0016] Through the above technical solution: the setting of the digital display frequency conversion speed regulator can control the speed of the frequency conversion reduction motor and make it convenient for the staff to observe the data.

[0017] The utility model is further configured that a constant temperature dropping funnel is fixedly connected to one side of the top of the enzymolysis tank body, and the constant temperature dropping funnel is communicated with the enzymolysis tank body.

[0018] Through the above technical solution: the setting of the constant temperature dropping funnel can control the dissolved liquid entering the enzymolysis tank.

[0019] The utility model is further configured such that a reflux device is fixedly connected to the other side of the top of the enzymolysis tank body, and the reflux device includes a collecting bottle, and the collecting bottle is fixedly connected to the enzymolysis tank body through an air pipe, and a communicating serpentine condenser is fixedly connected to the top of the collecting bottle.

[0020] Through the above technical solution: the setting of the reflux device can collect and process the steam in the enzymatic hydrolysis tank.

[0021] The beneficial effects of the utility model are:

[0022] 1. The high-temperature and high-pressure enzymolysis tank for feather meal production adds a dissolving liquid into the enzymolysis tank body through a constant-temperature dropping funnel, starts a variable-frequency reduction motor, and the output shaft of the variable-frequency reduction motor rotates to rotate the rotating shaft, and the rotation of the rotating shaft rotates the stirring rod, so that the raw material can be rotated, and the constant-temperature oil bath pot is started. The constant-temperature oil bath pot can be filled with water through an infusion tube through an inlet. After the interlayer is full, the water can be discharged through an outlet and circulated. With the detection of a glass thermometer, the raw material can be stirred at high temperature, enzymolysis can be performed at 4000 degrees, and hydrolysis can be performed at 4000 degrees. Therefore, the effect of improving the digestibility of the feather meal can be achieved.

[0023] 2. The high-temperature and high-pressure enzymolysis tank used for feather meal production can control the production temperature of feather meal through a glass thermometer, and can control the speed of the variable frequency reduction motor through a digital display variable frequency speed regulator, and is convenient for staff to observe the data. The dissolved liquid entering the enzymolysis tank body can be controlled through a constant temperature dropping funnel, and the steam in the enzymolysis tank body can be collected and processed through a reflux device. BRIEF DESCRIPTION OF THE DRAWINGS

[0024] Figure 1 This is a three-dimensional structural schematic diagram of a high-temperature and high-pressure enzymatic hydrolysis tank for feather meal production proposed by the utility model;

[0025] Figure 2 This is a partial cross-sectional structural schematic diagram of a high-temperature and high-pressure enzymatic hydrolysis tank for feather meal production proposed by the utility model;

[0026] Figure 3 for Figure 2 Schematic diagram of the enlarged structure at point A in the middle.

[0027] In the figure: 1. Enzyme hydrolysis tank; 2. Variable frequency reduction motor; 3. Rotating shaft; 4. Stirring rod; 5. Interlayer; 6. Inlet; 7. Constant temperature oil bath; 8. Base; 9. Connecting frame; 10. Glass thermometer; 11. Digital display variable frequency speed regulator; 12. Constant temperature dropping funnel; 13. Reflux device. DETAILED DESCRIPTION

[0028] The technical solution of this patent is further described in detail below in conjunction with specific implementation methods.

[0029] The embodiments of the present invention are described in detail below, and examples of the embodiments are shown in the accompanying drawings, wherein the same or similar reference numerals throughout represent the same or similar elements or elements having the same or similar functions. The embodiments described below with reference to the accompanying drawings are exemplary and are only used to explain the present invention, and cannot be understood as limiting the present invention.

[0030] In the description of this patent, it should be understood that the terms "center", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside", "outside", etc., indicating the orientation or position relationship, are based on the orientation or position relationship shown in the drawings, and are only for the convenience of describing this patent and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore cannot be understood as a limitation on this patent.

[0031] In the description of this patent, it should be noted that, unless otherwise clearly specified and limited, the terms "installed", "connected", "connected", and "set" should be understood in a broad sense, for example, it can be fixedly connected or set, or it can be detachably connected or set, or connected or set in one piece. For ordinary technicians in this field, the specific meanings of the above terms in this patent can be understood according to specific circumstances.

[0032] Reference Figure 1-3 A high-temperature and high-pressure enzymolysis tank for feather meal production comprises an enzymolysis tank body 1, a variable frequency reduction motor 2 is arranged on the top of the enzymolysis tank body 1, a rotating shaft 3 is fixedly connected to the output shaft of the variable frequency reduction motor 2, a stirring rod 4 is fixedly connected to the bottom of the rotating shaft 3, the stirring rod 4 is located in the enzymolysis tank body 1, an interlayer 5 is provided on the wall surface of the enzymolysis tank body 1, an inlet 6 is provided at the bottom of the outer wall on one side of the interlayer 5, an outlet is provided at the top of the outer wall on the other side of the interlayer 5, a constant temperature oil bath pot 7 is arranged on one side of the enzymolysis tank body 1, and the constant temperature oil bath pot 7 is fixedly connected to the inlet 6 and the outlet respectively through an infusion tube.

[0033] It should be noted that, in this embodiment, a base 8 is provided at the bottom of the enzymatic hydrolysis tank body 1, and a connecting frame 9 is fixedly connected to the top of the base 8. The connecting frame 9 is fixed to the variable frequency reduction motor 2 and the enzymatic hydrolysis tank body 1 by a connecting piece, and the base 8 can ensure smooth stirring.

[0034] Furthermore, in the present embodiment, the stirring rod 4 is made of polytetrafluoroethylene, which is resistant to high temperature, corrosion, high lubricity, and non-adhesive, so as to avoid interference with the feather powder.

[0035] A glass thermometer 10 is fixedly connected to the top of the enzymatic hydrolysis tank 1 , and a detection head of the glass thermometer 10 is close to the feather powder. The production temperature of the feather powder can be controlled by the glass thermometer 10 .

[0036] A digital display variable frequency speed regulator 11 is fixedly connected to the top of the connecting frame 9. The digital display variable frequency speed regulator 11 is connected to the variable frequency reduction motor 2 through electric wires. The digital display variable frequency speed regulator 11 can control the speed of the variable frequency reduction motor 2, and it is convenient for staff to observe the data.

[0037] A constant temperature dropping funnel 12 is fixedly connected to one side of the top of the enzymolysis tank body 1 . The constant temperature dropping funnel 12 is in communication with the enzymolysis tank body 1 . The dissolved liquid entering the enzymolysis tank body 1 can be controlled by the constant temperature dropping funnel 12 .

[0038] A reflux device 13 is fixedly connected to the other side of the top of the enzymolysis tank body 1. The reflux device 13 includes a collecting bottle. The collecting bottle is fixedly connected to the enzymolysis tank body 1 through a gas pipe. A connected serpentine condenser is fixedly connected to the top of the collecting bottle. The steam in the enzymolysis tank body 1 can be collected and processed through the reflux device 13.

[0039] Working principle: when in use, the raw material is added into the enzymolysis tank body 1, and then the dissolving liquid is added into the enzymolysis tank body 1 through the constant temperature dropping funnel 12, and the variable frequency reduction motor 2 is started. The output shaft of the variable frequency reduction motor 2 rotates to rotate the rotating shaft 3, and the rotation of the rotating shaft 3 rotates the stirring rod 4, so that the raw material can be rotated, and the constant temperature oil bath pot 7 is started. The constant temperature oil bath pot 7 can be filled with water through the inlet 6 through the infusion tube. After the interlayer 5 is filled, it can be discharged through the outlet and circulated. With the detection of the glass thermometer 10, the raw material can be stirred at high temperature, enzymolysis is carried out at 50 degrees, and hydrolysis is carried out at 150 degrees. Therefore, the effect of improving the digestibility of feather meal can be achieved.

[0040] The above description is only a preferred specific implementation manner of the present invention, but the protection scope of the present invention is not limited thereto. Any technician familiar with the technical field can make equivalent replacements or changes within the technical scope disclosed by the present invention according to the technical scheme and the utility model concept of the present invention, which should be covered by the protection scope of the present invention.

Claims

1. A high-temperature and high-pressure enzymolysis tank for feather meal production, comprising an enzymolysis tank body (1), characterized in that: A variable frequency reduction motor (2) is arranged on the top of the enzymolysis tank (1); the output shaft of the variable frequency reduction motor (2) is fixedly connected to a rotating shaft (3); the bottom of the rotating shaft (3) is fixedly connected to a stirring rod (4); the stirring rod (4) is located in the enzymolysis tank (1); a wall surface of the enzymolysis tank (1) is provided with an interlayer (5); an inlet (6) is arranged at the bottom of an outer wall on one side of the interlayer (5); an outlet is arranged at the top of an outer wall on the other side of the interlayer (5); a constant temperature oil bath (7) is arranged on one side of the enzymolysis tank (1); the constant temperature oil bath (7) is fixedly connected to the inlet (6) and the outlet respectively via an infusion tube.

2. The high temperature and high pressure enzymolysis tank for feather meal production according to claim 1, characterized in that: The bottom of the enzymolysis tank (1) is provided with a base (8), the top of the base (8) is fixedly connected with a connecting frame (9), and the connecting frame (9) is fixed to the variable frequency reduction motor (2) and the enzymolysis tank (1) via a connecting piece.

3. The high temperature and high pressure enzymolysis tank for feather meal production according to claim 1, characterized in that: The stirring rod (4) is made of polytetrafluoroethylene.

4. The high temperature and high pressure enzymolysis tank for feather meal production according to claim 1, characterized in that: A glass thermometer (10) is fixedly connected to the top of the enzymatic hydrolysis tank (1), and a detection head of the glass thermometer (10) is close to the feather powder.

5. The high temperature and high pressure enzymolysis tank for feather meal production according to claim 2, characterized in that: A digital display variable frequency speed regulator (11) is fixedly connected to the top of the connecting frame (9), and the digital display variable frequency speed regulator (11) is connected to the variable frequency reduction motor (2) via electric wires.

6. The high temperature and high pressure enzymolysis tank for feather meal production according to claim 1, characterized in that: A constant temperature dropping funnel (12) is fixedly connected to one side of the top of the enzymolysis tank (1), and the constant temperature dropping funnel (12) is connected to the enzymolysis tank (1).

7. The high temperature and high pressure enzymolysis tank for feather meal production according to claim 6, characterized in that: A reflux device (13) is fixedly connected to the other side of the top of the enzymolysis tank (1), and the reflux device (13) comprises a collecting bottle, and the collecting bottle is fixedly connected to the enzymolysis tank (1) via a gas pipe, and a communicating serpentine condenser is fixedly connected to the top of the collecting bottle.

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