Collagen peptide concentrated solution concentration equipment

Abstract

The utility model relates to the technical field of concentration equipment, in particular to collagen peptide concentrated solution concentration equipment, which comprises a distillation retort, a circulation mechanism is mounted on the wall of the distillation retort, and the circulation mechanism is formed by combining a hollow tank, a thermocouple heating disc, a heat preservation pipe, a steam exhaust pipe, a steam pipe, a connecting plate and a condensate water drainage pipe. A hollow tank is welded to the inner wall of the distillation tank through a connecting plate, a steam pipe is installed on the side wall of the hollow tank in a communicating mode, the other end of the steam pipe is connected with the single-layer side wall of the hollow tank in a communicating mode, a heat preservation pipe is connected to the tank wall of the steam pipe in a sleeving mode, and a thermocouple heating disc is installed at the tank bottom of the hollow tank; and the water vapor is discharged into the hollow side wall of the hollow tank to heat the hollow tank, so that the power of the thermocouple heating disc is reduced, and the energy consumption is reduced.

Description

Technical Field

[0001] The utility model relates to the technical field of concentration equipment, in particular to a concentration equipment for collagen peptide concentrated solution. Background Technique

[0002] The production process of soybean peptide powder, corn oligopeptide powder, rice peptide powder and wheat oligopeptide powder involves multiple steps from raw material selection to pretreatment, enzymatic hydrolysis and separation and purification. Among them, the enzymatic hydrolysis process is the key link, which directly affects the quality and yield of the final product. When concentrating the concentrated solution of soybean peptide powder, corn oligopeptide powder, rice peptide powder and wheat oligopeptide powder, it is necessary to add an appropriate amount of water to the raw materials of soybean peptide powder, corn oligopeptide powder, rice peptide powder and wheat oligopeptide powder and mix them. After high-temperature steaming and under suitable pH conditions, an appropriate amount of enzyme hydrolyzing agent is added, and after enzymatic hydrolysis extraction, the concentrated solution is concentrated. After completion, fine filtration and drying are carried out to form collagen peptide powder.

[0003] Currently, when concentrating the concentrated solution of soybean peptide powder, corn oligopeptide powder, rice peptide powder and wheat oligopeptide powder, a distillation tank is usually used for distillation and concentration. However, when the existing distillation tank is distilling, the generated water vapor contains relatively high heat. Directly discharging the water vapor causes the heat of the water vapor to be unable to be utilized, increasing the energy consumption during distillation. For this reason, we propose a concentration equipment for collagen peptide concentrated solution to facilitate reducing energy consumption during distillation and concentration. Summary of the Utility Model

[0004] Aiming at the problems in the prior art, the utility model provides a concentration equipment for collagen peptide concentrated solution.

[0005] The technical solution adopted by the utility model to solve its technical problems is a concentration equipment for collagen peptide concentrated solution, including a distillation tank. A circulation mechanism is installed at the tank wall of the distillation tank. The circulation mechanism is composed of a hollow tank, a thermocouple heating plate, a heat preservation pipe, an exhaust pipe, a steam pipe, a connecting plate and a condensate drain pipe. The hollow tank is welded and connected to the inner wall of the distillation tank through the connecting plate. A steam pipe is communicated and installed at the side wall of the hollow tank. The other end of the steam pipe is communicated and connected to the single-layer side wall of the hollow tank. A heat preservation pipe is sleeved on the tank wall of the steam pipe. A thermocouple heating plate is installed at the bottom of the hollow tank. An exhaust pipe is communicated and installed at the single-layer side wall of the hollow tank. A condensate drain pipe is communicated and installed at the single-layer side wall of the hollow tank. The hollow tank is a double-layer structure with a hollow side wall, and its top and bottom are both single-layer structures.

[0006] By adopting the above technical solution, when reducing the energy consumption of the distillation concentrate, since a circulation mechanism is installed at the tank wall of the distillation tank, the circulation mechanism is composed of a hollow tank, a thermocouple heating plate, a heat preservation pipe, an exhaust pipe, a steam pipe, a connecting plate and a condensate drain pipe. The thermocouple heating plate at the bottom of the hollow tank is heated by a controller. When the temperature in the hollow tank rises and water vapor is generated, the water vapor is discharged through the steam pipe. A heat preservation pipe is sleeved on the tank wall of the steam pipe to keep it warm. The other end of the steam pipe is connected and communicated with the single-layer side wall of the hollow tank, so as to discharge the water vapor into the hollow side wall of the hollow tank to heat the hollow tank, realizing the reduction of the power of the thermocouple heating plate and the reduction of energy consumption. The condensate in the hollow side wall of the hollow tank is discharged through the condensate drain pipe, and the water vapor at the hollow side wall of the hollow tank is discharged through the exhaust pipe.

[0007] Specifically, it further includes a discharging mechanism, and a discharging mechanism is installed at the tank wall of the hollow tank.

[0008] By adopting the above technical solution, the concentrated liquid after distillation can be conveniently discharged through the discharging mechanism.

[0009] Specifically, the discharging mechanism is composed of a motor, a rotating shaft, a collar, blades, a shearing screw and a peptide discharging valve pipe. The motor is installed at the top of the distillation tank through bolts. The output end of the motor is installed with a rotating shaft. The rotating shaft is located inside the hollow tank. A group of symmetric collars are fixedly installed on the shaft wall of the rotating shaft. Blades are installed on the ring walls of a group of collars. The other end of the rotating shaft is installed with a shearing screw. The peptide discharging valve pipe is communicated and installed at the bottom of the tank of the hollow tank. The shearing screw is located inside the peptide discharging valve pipe.

[0010] By adopting the above technical solution, when discharging the concentrated liquid of soybean peptide powder, corn oligopeptide powder, rice peptide powder and wheat oligopeptide powder after concentration, since a discharging mechanism is installed at the tank wall of the hollow tank, and the discharging mechanism is composed of a motor, a rotating shaft, a collar, blades, a shearing screw and a peptide discharging valve pipe. The motor is controlled by a controller, so that the motor drives the rotating shaft at its output end to rotate. The rotating shaft drives the collars and blades to stir inside the hollow tank, improving the distillation efficiency of the concentrated liquid. After the operator opens the peptide discharging valve pipe at the bottom of the hollow tank, since the other end of the rotating shaft is installed with a shearing screw and the shearing screw is located inside the peptide discharging valve pipe, when the operator opens the peptide discharging valve pipe, it is convenient to discharge the concentrated liquid after distillation.

[0011] Specifically, a liquid inlet valve pipe is communicated and installed at the side wall of the hollow tank, and a funnel is installed at the other end of the liquid inlet valve pipe.

[0012] By adopting the above technical solution, it is convenient to add the hydrolyzed stock solutions of soybean peptide powder, corn oligopeptide powder, rice peptide powder and wheat oligopeptide powder into the liquid inlet valve pipe through the funnel, and it is convenient to inject the hydrolyzed stock solution into the hollow tank through the liquid inlet valve pipe.

[0013] Specifically, a controller for controlling the motor and the thermocouple heating plate is installed at the tank wall of the distillation tank.

[0014] By adopting the above technical solution, it is convenient to control the motor and the thermocouple heating plate through the controller.

[0015] Beneficial effects of the present utility model:

[0016] (1) For the collagen peptide concentrate equipment of the present utility model, when reducing the energy consumption of the distilled concentrate, since a circulation mechanism is installed at the tank wall of the distillation tank, the circulation mechanism is composed of a hollow tank, a thermocouple heating plate, a heat preservation pipe, an exhaust pipe, a steam pipe, a connecting plate and a condensate drain pipe. The thermocouple heating plate at the bottom of the hollow tank is heated through the controller. When the temperature in the hollow tank rises and water vapor is generated, the water vapor is discharged through the steam pipe. A heat preservation pipe is sleeved on the tank wall of the steam pipe to keep it warm. The other end of the steam pipe is connected and communicated with the single-layer side wall of the hollow tank, so as to discharge the water vapor into the hollow side wall of the hollow tank to heat the hollow tank, realizing the reduction of the power of the thermocouple heating plate and the reduction of energy consumption. The condensate in the hollow side wall of the hollow tank is discharged through the condensate drain pipe, and the water vapor at the hollow side wall of the hollow tank is discharged through the exhaust pipe.

[0017] (2) For the collagen peptide concentrate equipment of the present utility model, when discharging the concentrated solutions of soybean peptide powder, corn oligopeptide powder, rice peptide powder and wheat oligopeptide powder after concentration, since a discharging mechanism is installed at the tank wall of the hollow tank, the discharging mechanism is composed of a motor, a rotating shaft, a collar, blades, a shearing screw and a peptide discharging valve pipe. The motor is controlled through the controller, so that the motor drives the rotating shaft at its output end to rotate. The rotating shaft drives the collar and the blades to stir in the hollow tank, improving the distillation efficiency of the concentrate. After the operator opens the peptide discharging valve pipe at the bottom of the hollow tank, since a shearing screw is installed at the other end of the rotating shaft and the shearing screw is located in the peptide discharging valve pipe, when the operator opens the peptide discharging valve pipe, it is convenient to discharge the distilled concentrate. Description of the drawings

[0018] The present utility model will be further described below with reference to the drawings and embodiments.

[0019] Figure 1 is the main drawing of the present utility model;

[0020] Figure 2 is the schematic structural diagram of the circulation mechanism of the present utility model;

[0021] Figure 3 is the schematic structural diagram of the discharging mechanism of the present utility model;

[0022] In the figure: 1, distillation tank; 2, circulation mechanism; 201, hollow tank; 202, thermocouple heating plate; 203, heat preservation pipe; 204, exhaust pipe; 205, steam pipe; 206, connecting plate; 207, condensate drain pipe; 3, controller; 4, discharging mechanism; 401, motor; 402, rotating shaft; 403, collar; 404, blade; 405, shearing screw; 406, slag discharge valve pipe; 5, funnel; 6, liquid inlet valve pipe. Specific embodiments

[0023] In order to make the technical means, creative features, achieved purposes and functions of the present utility model easy to understand, the present utility model will be further described below in conjunction with specific embodiments.

[0024] As an embodiment of the present utility model, as Figure 1 、 Figure 2 and Figure 3 shown, a collagen peptide concentrate concentration device described in the present utility model includes a distillation tank 1. A circulation mechanism 2 is installed at the tank wall of the distillation tank 1. The circulation mechanism 2 is composed of a hollow tank 201, a thermocouple heating plate 202, a heat preservation pipe 203, an exhaust pipe 204, a steam pipe 205, a connecting plate 206 and a condensate drain pipe 207. A hollow tank 201 is welded and connected to the inner wall of the distillation tank 1 through a connecting plate 206. A steam pipe 205 is communicated and installed at the side wall of the hollow tank 201. The other end of the steam pipe 205 is communicated and connected to the single-layer side wall of the hollow tank 201. A heat preservation pipe 203 is sleeved on the tank wall of the steam pipe 205. A thermocouple heating plate 202 is installed at the bottom of the hollow tank 201. An exhaust pipe 204 is communicated and installed at the single-layer side wall of the hollow tank 201. A condensate drain pipe 207 is communicated and installed at the single-layer side wall of the hollow tank 201. The hollow tank 201 is a double-layer structure with a hollow side wall, and its top and bottom are both single-layer structures.

[0025] In use, when reducing the energy consumption of the distillation concentrate, since a circulation mechanism 2 is installed at the tank wall of the distillation tank 1, the circulation mechanism 2 is composed of a hollow tank 201, a thermocouple heating plate 202, a heat preservation pipe 203, an exhaust pipe 204, a steam pipe 205, a connecting plate 206 and a condensate drain pipe 207. The thermocouple heating plate 202 at the bottom of the hollow tank 201 is heated by a controller 3. When the temperature in the hollow tank 201 rises and water vapor is generated, the water vapor is discharged through the steam pipe 205. A heat preservation pipe 203 is sleeved on the tank wall of the steam pipe 205 to keep it warm. The other end of the steam pipe 205 is connected and communicated with the single-layer side wall of the hollow tank 201, so as to discharge the water vapor into the hollow side wall of the hollow tank 201 to heat the hollow tank 201, realizing the reduction of the power of the thermocouple heating plate 202 and the reduction of energy consumption. The condensate in the hollow side wall of the hollow tank 201 is discharged through the condensate drain pipe 207, and the water vapor at the hollow side wall of the hollow tank 201 is discharged through the exhaust pipe 204.

[0026] As Figure 1 shown, it further includes a discharging mechanism 4, and the discharging mechanism 4 is installed at the tank wall of the hollow tank 201.

[0027] In use, the concentrated liquid after distillation can be conveniently discharged through the discharging mechanism 4.

[0028] As Figure 1 and Figure 3 shown, the discharging mechanism 4 is composed of a motor 401, a rotating shaft 402, a collar 403, blades 404, a shearing screw 405 and a peptide discharging valve pipe 406. The motor 401 is installed at the top of the distillation tank 1 through bolts. The output end of the motor 401 is installed with a rotating shaft 402. The rotating shaft 402 is located inside the hollow tank 201. A group of symmetric collars 403 are fixedly installed on the shaft wall of the rotating shaft 402. Blades 404 are installed on the ring walls of a group of collars 403. The other end of the rotating shaft 402 is installed with a shearing screw 405. The peptide discharging valve pipe 406 is communicated and installed at the bottom of the hollow tank 201. The shearing screw 405 is located inside the peptide discharging valve pipe 406.

[0029] During use, when the concentrated solutions of soybean peptide powder, corn oligopeptide powder, rice peptide powder, and wheat oligopeptide powder are discharged after concentration, since a discharging mechanism 4 is installed at the tank wall of the hollow tank 201, the discharging mechanism 4 is composed of a motor 401, a rotating shaft 402, a collar 403, blades 404, a shearing screw 405, and a peptide discharging valve pipe 406. By controlling the motor 401 through the controller 3, the motor 401 drives the rotating shaft 402 at its output end to rotate. The rotating shaft 402 drives the collar 403 and the blades 404 to stir inside the hollow tank 201, improving the distillation efficiency of the concentrated solution. After the personnel open the peptide discharging valve pipe 406 at the bottom of the hollow tank 201, since the shearing screw 405 is installed at the other end of the rotating shaft 402 and the shearing screw 405 is located inside the peptide discharging valve pipe 406, when the personnel open the peptide discharging valve pipe 406, it is convenient to discharge the distilled concentrated solution.

[0030] As Figure 2 shown, a liquid inlet valve pipe 6 is connected and installed at the side wall of the hollow tank 201, and a funnel 5 is installed at the other end of the liquid inlet valve pipe 6.

[0031] During use, it is convenient to add the hydrolyzed stock solutions of soybean peptide powder, corn oligopeptide powder, rice peptide powder, and wheat oligopeptide powder into the liquid inlet valve pipe 6 through the funnel 5, and it is convenient to inject the hydrolyzed stock solution into the hollow tank 201 through the liquid inlet valve pipe 6.

[0032] As Figure 1 shown, a controller 3 for controlling the motor 401 and the thermocouple heating plate 202 is installed at the tank wall of the distillation tank 1.

[0033] During use, it is convenient to control the motor 401 and the thermocouple heating plate 202 through the controller 3.

[0034] When the present utility model is in use, when reducing the energy consumption of the distillation concentrate, since a circulation mechanism 2 is installed at the tank wall of the distillation tank 1, the circulation mechanism 2 is composed of a hollow tank 201, a thermocouple heating plate 202, a heat preservation pipe 203, an exhaust pipe 204, a steam pipe 205, a connecting plate 206 and a condensate drain pipe 207. The thermocouple heating plate 202 at the bottom of the hollow tank 201 is heated through the controller 3. When the temperature in the hollow tank 201 rises and water vapor is generated, the water vapor is discharged through the steam pipe 205. A heat preservation pipe 203 is sleeved on the tank wall of the steam pipe 205 to keep it warm. The other end of the steam pipe 205 is connected and communicated with the single-layer side wall of the hollow tank 201, so as to discharge the water vapor into the hollow side wall of the hollow tank 201 to heat the hollow tank 201, realizing the reduction of the power of the thermocouple heating plate 202 and the reduction of energy consumption. The condensate in the hollow side wall of the hollow tank 201 is discharged through the condensate drain pipe 207, and the water vapor at the hollow side wall of the hollow tank 201 is discharged through the exhaust pipe 204. When discharging the concentrated solutions of soybean peptide powder, corn oligopeptide powder, rice peptide powder and wheat oligopeptide powder after concentration, since a discharging mechanism 4 is installed at the tank wall of the hollow tank 201, the discharging mechanism 4 is composed of a motor 401, a rotating shaft 402, a collar 403, blades 404, a shearing screw 405 and a peptide discharging valve pipe 406. The motor 401 is controlled through the controller 3, so that the motor 401 drives the rotating shaft 402 at its output end to rotate. The rotating shaft 402 drives the collar 403 and the blades 404 to stir in the hollow tank 201, improving the distillation efficiency of the concentrated solution. After the operator opens the peptide discharging valve pipe 406 at the bottom of the hollow tank 201, since a shearing screw 405 is installed at the other end of the rotating shaft 402 and the shearing screw 405 is located in the peptide discharging valve pipe 406, when the operator opens the peptide discharging valve pipe 406, it is convenient to discharge the distilled concentrated solution.

[0035] The controller is an electrical control box, and a Siemens PLC control unit is arranged inside. A touch screen is arranged at the door panel. The output end of the touch screen is electrically connected to the input end of the PLC control unit. The input ends of the motor and the thermocouple heating plate are electrically connected to the output end of the Siemens PLC controller, realizing the control of the motor and the thermocouple heating plate.

[0036] The above shows and describes the basic principles, main features and advantages of the present utility model. Those skilled in the art of this industry should understand that the present utility model is not limited by the above embodiments. The above embodiments and the descriptions in the specification only illustrate the principles of the present utility model. Without departing from the spirit and scope of the present utility model, the present utility model will have various changes and improvements, and these changes and improvements all fall within the scope of protection required by the present utility model. The scope of protection required by the present utility model is defined by the appended claims and their equivalents.

Claims

1. A collagen peptide concentrate equipment, characterized in that: It includes a distillation tank (1), and a circulation mechanism (2) is installed at the tank wall of the distillation tank (1). The circulation mechanism (2) is composed of a hollow tank (201), a thermocouple heating plate (202), a heat preservation pipe (203), an exhaust pipe (204), a steam pipe (205), a connecting plate (206) and a condensate drain pipe (207). The hollow tank (201) is welded and connected to the inner wall of the distillation tank (1) through the connecting plate (206). A steam pipe (205) is connected and installed at the side wall of the hollow tank (201). The other end of the steam pipe (205) is connected and communicated with the single-layer side wall of the hollow tank (201). A heat preservation pipe (203) is sleeved on the tank wall of the steam pipe (205). A thermocouple heating plate (202) is installed at the bottom of the hollow tank (201). An exhaust pipe (204) is connected and installed at the single-layer side wall of the hollow tank (201). A condensate drain pipe (207) is connected and installed at the single-layer side wall of the hollow tank (201). The hollow tank (201) is a double-layer structure with a hollow side wall, and its top and bottom are both single-layer structures.

2. The collagen peptide concentrate equipment according to claim 1, characterized in that: It further includes a discharging mechanism (4), and the discharging mechanism (4) is installed at the tank wall of the hollow tank (201).

3. The collagen peptide concentrate equipment according to claim 2, wherein: The discharging mechanism (4) is composed of a motor (401), a rotating shaft (402), a collar (403), blades (404), a shearing screw (405) and a peptide discharging valve pipe (406). The motor (401) is installed at the top of the distillation tank (1) through bolts. The output end of the motor (401) is installed with the rotating shaft (402). The rotating shaft (402) is located inside the hollow tank (201). A group of symmetric collars (403) are fixedly installed on the shaft wall of the rotating shaft (402). Blades (404) are installed on the ring walls of the group of collars (403). The other end of the rotating shaft (402) is installed with the shearing screw (405). The peptide discharging valve pipe (406) is connected and installed at the bottom of the hollow tank (201). The shearing screw (405) is located inside the peptide discharging valve pipe (406).

4. A collagen peptide concentrate equipment according to claim 1, characterized in that: A liquid inlet valve pipe (6) is connected and installed at the side wall of the hollow tank (201), and a funnel (5) is installed at the other end of the liquid inlet valve pipe (6).

5. The collagen peptide concentrate equipment according to claim 1, characterized in that: A controller (3) for controlling the motor (401) and the thermocouple heating plate (202) is installed at the tank wall of the distillation tank (1).

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