Automatic batter beater
By introducing automatic powder replenishment, water supply and stirring functions into the baking bead beater, combined with precise control and multi-speed stirring device, the problem of low degree of automation of the baking bead machine is solved, and efficient and stable baking production is achieved.
Patent Information
- Application Number
- CN202422306062.7
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-09-21
- Publication Date
- 2025-07-22
- Estimated Expiration
- 2034-09-21
AI Technical Summary
The existing slurry beating machines have low automation and inaccurate supply of powder and water, resulting in unstable slurry quality. The slurry and concentrated slurry are completed by different machines respectively, increasing equipment investment.
An automatic matte beater is designed, including powder filling device, water supply device and agitator. It uses a weighing sensor and a flowmeter to accurately control the amount of powder and water. It combines a high-speed and low-speed stirring device and is equipped with a cooling system and a temperature sensor to achieve automated control.
It improves the beating efficiency and slurry quality stability, reduces manual operation requirements, reduces costs, and can produce slurries of different viscosity, achieving multiple uses in one machine.
Smart Images

Figure CN223125707U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of food machinery, and particularly relates to an automatic slurry beater for noodles. Background Art
[0002] The slurry beater for noodles is one of the important devices designed for the processing production line of conditioned meat products, and its purpose is to ensure the stable quality of the slurry of the sizing device.
[0003] At present, the slurry beater for noodles is in a semi-automatic state and can automatically complete the functions of stirring and pumping slurry. However, the supply of powder and water in the early stage is generally completed manually, and the measurement is inaccurate; the cooling system is mostly cooled by ice flakes in the interlayer, and the temperature control is unstable, resulting in unstable physical and chemical indexes of the slurry, which are all factors causing unstable slurry quality. In addition, the thin slurry and the thick slurry are completed by different machines respectively, increasing the equipment investment. Summary of the Utility Model
[0004] Aiming at the above deficiencies, the technical problem to be solved by the utility model is to provide an automatic slurry beater for noodles that can automatically supply water, powder and stir, with high automation degree and high stirring efficiency.
[0005] To solve the above technical problem, the technical solution of the utility model is:
[0006] An automatic slurry beater for noodles, comprising: a frame, on which a beating barrel, a stirring device, a powder replenishing device and a water supply device are arranged;
[0007] The powder replenishing device includes a powder box, a mesh belt conveyor, a weighing frame and a weighing sensor. The discharging end of the mesh belt conveyor is located above the beating barrel. The mesh belt conveyor is located below the discharging port of the powder box. A powder supporting plate is arranged below the upper belt of the mesh belt conveyor. The powder box and the mesh belt conveyor are installed on the weighing frame, and the weighing sensor is arranged at the lower part of the weighing frame;
[0008] The water supply device includes a water supply pipe, a flow meter and a water supply solenoid valve arranged on the water supply pipe. The water supply pipe is used for supplying water to the beating barrel.
[0009] Preferably, a gate adjusting device is arranged above the upper belt of the mesh belt conveyor. The gate adjusting device includes an electric actuator, a connecting rod, two limit seats and a vertically slidable gate plate. The gate plate is arranged along the width direction of the mesh belt conveyor. The two limit seats are relatively and fixedly arranged on the gate plate. One end of the connecting rod is connected to the electric actuator, and the other end is provided with a ball head, and the ball head is located between the two limit seats.
[0010] Preferably, the stirring device includes a high-speed stirring device and a low-speed stirring device.
[0011] Preferably, the high-speed stirring device includes a high-speed motor and high-speed stirring blades driven by the high-speed motor, and the high-speed stirring blades extend into the bottom of the pulping barrel.
[0012] The low-speed stirring device includes a low-speed motor and low-speed stirring blades driven by the low-speed motor, and the low-speed stirring blades extend into the bottom of the pulping barrel and are close to the barrel wall of the pulping barrel.
[0013] Preferably, the pulping barrel is provided with a cooling device, and the cooling device includes a cooling channel, a coolant inlet pipe, a coolant outlet pipe and a cooling solenoid valve. The cooling channel is arranged in the interlayer of the barrel wall of the pulping barrel and is spiral around the center of the pulping barrel. The coolant inlet pipe is communicated with one end of the cooling channel, the coolant outlet pipe is communicated with the other end of the cooling channel, and the cooling solenoid valve is arranged on the coolant inlet pipe.
[0014] Preferably, the cooling medium in the cooling device is ethylene glycol.
[0015] Preferably, the pulping barrel is provided with a temperature sensor.
[0016] Preferably, the bottom of the pulping barrel is wedge-shaped, a pulp outlet is arranged at the lowest part of the bottom of the pulping barrel, and the temperature sensor is arranged at the pulp outlet.
[0017] Preferably, the pulping barrel is connected with a pulp conveying device, and the pulp conveying device includes a pulp conveying pipe connected with the pulp outlet and a pulp conveying pump arranged on the pulp conveying pipe.
[0018] Preferably, an on-line viscometer is arranged at the bottom of the pulping barrel.
[0019] After adopting the above technical solution, the beneficial effects of the present utility model are as follows:
[0020] The automatic noodle pulp pulping machine of the present application has functions of automatic powder feeding, water feeding and stirring, with high automation degree, greatly improving the pulping efficiency, requiring fewer operators, reducing costs, and the water feeding amount and powder feeding amount can be accurately controlled, and noodle pulp with different viscosities, such as thin pulp or thick pulp, etc., can be obtained, achieving the purpose of multi-purpose use of one machine and reducing equipment investment. Description of the Drawings
[0021] Figure 1 is a three-dimensional structural schematic diagram of an embodiment of the automatic noodle pulp pulping machine of the present utility model;
[0022] Figure 2 is a side view structural schematic diagram of an embodiment of the automatic noodle pulp pulping machine of the present utility model;
[0023] Figure 3It is a schematic side view structure diagram of another direction of the embodiment of the automatic noodle pulp beater of the present utility model;
[0024] Figure 4 It is a schematic structure diagram of the powder supplement device;
[0025] Figure 5 It is Figure 4 An enlarged schematic structure diagram of part A in
[0026] Figure 6 It is a schematic structure diagram of the stirring device;
[0027] Figure 7 It is a schematic structure diagram of the water supply device;
[0028] Figure 8 It is a schematic structure diagram of the cooling device;
[0029] Figure 9 It is a schematic structure diagram of the pulp conveying device;
[0030] Figure 10 It is a working schematic diagram of the embodiment of the automatic noodle pulp beater of the present utility model;
[0031] In the figure: 1, frame; 2, beating barrel; 3, stirring device; 311, high-speed motor; 312, high-speed stirring blade; 321, low-speed motor; 322, low-speed stirring blade; 4, powder supplement device; 41, powder box; 42, mesh belt conveyor; 421, powder supporting plate; 43, weighing frame; 44, weighing sensor; 45, gate adjusting device; 451, electric actuator; 452, connecting rod; 453, limit seat; 454, gate plate; 455, ball head; 5, water supply device; 51, water supply pipe; 52, flow meter; 53, water supply solenoid valve; 6, cooling device; 61, coolant inlet pipe; 62, coolant outlet pipe; 63, cooling solenoid valve; 7, temperature sensor; 8, pulp conveying device; 81, pulp conveying pipe; 82, pulp conveying pump; 9, on-line viscometer; 10, electric control cabinet. Detailed implementation manners
[0032] In order to make the purpose, technical solutions and advantages of the present utility model clearer, the following further details the present utility model in conjunction with the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are only used to explain the present utility model and are not used to limit the present utility model.
[0033] As Figures 1 - 3 As commonly shown, an automatic noodle pulp beater includes: a frame 1, and a beating barrel 2, a stirring device 3, a powder supplement device 4 and a water supply device 5 are arranged on the frame 1.
[0034] As Figure 4As shown, the powder replenishing device 4 includes a powder bin 41, a mesh belt conveyor 42, a weighing frame 43 and a weighing sensor 44. The discharging end of the mesh belt conveyor 42 is located above the pulping vat 2. The mesh belt conveyor 42 is located below the discharging port of the powder bin 2. A powder supporting plate 421 is arranged below the upper belt of the mesh belt conveyor 42. The powder bin 41 and the mesh belt conveyor 42 are installed on the weighing frame 43, and the weighing sensor 44 is arranged at the lower part of the weighing frame 43.
[0035] As Figure 7 shown, the water supply device 5 includes a water supply pipe 51, a flow meter 52 and a water supply solenoid valve 53 arranged on the water supply pipe 51. The water supply pipe 51 is used to supply water to the pulping vat 2.
[0036] As Figure 10 shown, when pulping the dough paste, the water supply solenoid valve 53 is opened, and the water supply pipe 51 supplies water to the pulping vat 2. The flow meter 52 detects the supplied water volume. When the supplied water volume reaches the set value, the water supply solenoid valve 53 is closed to stop the water supply. The weighing sensor 44 detects the initial weight W1 of the powder bin 41 and the mesh belt conveyor 42. The mesh belt conveyor 42 operates to convey the flour in the powder bin 41 into the pulping vat 2. The weighing sensor 44 detects the real-time weight W2 of the powder bin 41 and the mesh belt conveyor 42. W = W1 - W2, and W is the weight of the flour conveyed into the pulping vat 2. When W reaches the set value, the mesh belt conveyor 42 stops operating. At the same time, the stirring device 3 operates to quickly stir the flour and water to obtain the dough paste with the required viscosity, and the uniformity of the dough paste is good.
[0037] The automatic dough paste pulping machine of the present application has functions of automatic powder replenishment, water supply and stirring, with high automation degree, greatly improving the pulping efficiency, requiring fewer operators, reducing the cost, and the water supply volume and powder replenishment volume are accurate, and different viscosities of dough paste, such as thin paste or thick paste, etc., can be accurately obtained, achieving the purpose of multi-purpose of one machine and reducing equipment investment.
[0038] As Figure 5As shown in the figure, if the powder replenishment is too fast, the flour is likely to form lumps during stirring. Above the upper belt of the mesh belt conveyor 42, there is a gate adjustment device 45 for controlling the powder replenishment flow rate. The gate adjustment device includes an electric actuator 451, a connecting rod 452, two limit seats 453, and a gate plate 454 vertically slidably arranged on the powder bin 41. The gate plate 454 is arranged along the width direction of the mesh belt conveyor 42. The two limit seats 453 are relatively spaced and fixed on the gate plate 454. One end of the connecting rod 452 is connected to the electric actuator 451, and the other end is provided with a ball head 455. The ball head 455 is located between the two limit seats 453, and the ball head 455 and the two limit seats 453 form a spherical hinge structure. When the electric actuator 451 drives the connecting rod 452 to rotate by a certain angle, the connecting rod 452 pushes the gate plate 454 to move up and down through the ball head 455 and the two limit seats 453, thereby adjusting the distance between the gate plate 454 and the upper belt of the mesh belt conveyor 42, adjusting the powder replenishment flow rate, enabling the flour to be loosely output and gradually added into the beating bucket 2, avoiding agglomeration during stirring, and facilitating stirring.
[0039] As Figure 6 shown in the figure, to improve the beating efficiency, the stirring device 3 includes a high-speed stirring device and a low-speed stirring device.
[0040] The high-speed stirring device includes a high-speed motor 311 and high-speed stirring blades 312 driven by the high-speed motor 311. The high-speed stirring blades 312 extend into the bottom of the beating bucket 2; the low-speed stirring device includes a low-speed motor 321 and low-speed stirring blades 322 driven by the low-speed motor 321. The low-speed stirring blades 322 extend into the bottom of the beating bucket 2 and are close to the barrel wall of the beating bucket 2, facilitating the cleaning and scraping of the flour adhering to the barrel wall.
[0041] During beating, the high-speed stirring device and the low-speed stirring device work simultaneously. The high-speed stirring blades 312 driven by the high-speed motor 311 rotate, and the low-speed stirring blades 322 driven by the low-speed motor 321 rotate, achieving the purpose of quickly stirring evenly and having a high beating efficiency. After the slurry is stirred evenly, the high-speed stirring device stops working, and the low-speed stirring device continues to stir to prevent the slurry from settling.
[0042] As Figure 8 shown in the figure, when the slurry is stirred, the slurry needs to be maintained at a certain temperature to ensure the physical and chemical indexes of the slurry. The beating bucket 2 is provided with a cooling device 6. The cooling device 6 includes a cooling channel, a coolant inlet pipe 61, a coolant outlet pipe 62, and a cooling solenoid valve 63. The cooling channel is arranged in the sandwich layer of the barrel wall of the beating bucket 2 and is spiral around the center of the beating bucket 2. The coolant inlet pipe 61 is communicated with one end of the cooling channel, the coolant outlet pipe 62 is communicated with the other end of the cooling channel, and the cooling solenoid valve 63 is arranged on the coolant inlet pipe 61. The cooling medium in the cooling device 6 is preferably ethylene glycol.
[0043] When the slurry is stirred, ethylene glycol enters the cooling channel from the coolant inlet pipe 61, and then flows back from the coolant outlet pipe 62, realizing the circulation of ethylene glycol. During the circulation process, ethylene glycol takes away the heat of the slurry and reduces the temperature of the slurry. The opening of the cooling solenoid valve 63 is adjusted according to the temperature of the slurry, and the flow rate of ethylene glycol is adjusted to keep the slurry at a certain temperature and ensure the physical and chemical indicators of the slurry.
[0044] Furthermore, the beating barrel 2 is provided with a temperature sensor 7, which detects the temperature of the slurry in real time and automatically adjusts the opening of the cooling solenoid valve 63 according to the temperature of the slurry.
[0045] To facilitate the output of the slurry, the bottom of the beating barrel 2 is wedge-shaped, and a slurry outlet is provided at the lowest point of the bottom of the beating barrel 2, and a temperature sensor 7 is provided at the slurry outlet. When the slurry is output, the real-time temperature of the slurry can still be detected to ensure the output temperature of the slurry.
[0046] like Figure 9 As shown, the beating barrel 2 is connected to a slurry delivery device 8, which includes a slurry delivery pipe 81 connected to the slurry outlet and a slurry delivery pump 82 arranged on the slurry delivery pipe 81. When delivering slurry, the slurry delivery pump 82 is started, and the slurry delivery pump 82 works to extract the slurry in the beating barrel 2 and transport it to the next process through the slurry delivery pipe 81.
[0047] An online viscometer 9 is provided at the bottom of the beating barrel 2, and the online viscometer 9 detects the viscosity of the slurry in real time. When the viscosity deviation is large, the water supply amount or the powder replenishment amount is adjusted to ensure the quality of the slurry.
[0048] An electric control cabinet 10 for controlling the automatic operation of the beater is arranged on the frame 1 .
[0049] The above are examples of the best implementation methods of the utility model, and the parts not described in detail are common knowledge of ordinary technicians in this field. The protection scope of the utility model shall be based on the content of the claims, and any equivalent transformation based on the technical enlightenment of the utility model is also within the protection scope of the utility model.
Claims
1. An automatic pulp beater, characterized in that, Comprising: A frame, on which a beating barrel, a stirring device, a powder supplementing device and a water feeding device are provided; The powder supplementing device includes a powder box, a mesh belt conveyor, a weighing rack and a weighing sensor. The discharging end of the mesh belt conveyor is located above the beating barrel. The mesh belt conveyor is located below the discharging opening of the powder box. A powder supporting plate is provided below the upper belt of the mesh belt conveyor. The powder box and the mesh belt conveyor are installed on the weighing rack, and the weighing sensor is arranged at the lower part of the weighing rack; The water feeding device includes a water feeding pipe, and a flowmeter and a water feeding solenoid valve arranged on the water feeding pipe. The water feeding pipe is used for feeding water to the beating barrel.
2. The automatic pulp beater according to claim 1, wherein, Above the upper belt of the mesh belt conveyor, there is a gate adjusting device, which includes an electric actuator, a connecting rod, two limit seats and a vertically slidable gate plate. The gate plate is arranged along the width direction of the mesh belt conveyor. The two limit seats are fixedly arranged opposite to each other at intervals on the gate plate. One end of the connecting rod is connected to the electric actuator, and the other end is provided with a ball head, which is located between the two limit seats.
3. The automatic pulp beater according to claim 1, characterized in that, The stirring device includes a high-speed stirring device and a low-speed stirring device.
4. The automatic pulp beater according to claim 3, characterized in that, The high-speed stirring device includes a high-speed motor and high-speed stirring blades driven by the high-speed motor. The high-speed stirring blades extend into the bottom of the beating barrel; The low-speed stirring device includes a low-speed motor and low-speed stirring blades driven by the low-speed motor. The low-speed stirring blades extend into the bottom of the beating barrel and are close to the barrel wall of the beating barrel.
5. The automatic pulp beater according to claim 1, characterized in that, The beating barrel is provided with a cooling device, which includes a cooling channel, a coolant inlet pipe, a coolant outlet pipe and a cooling solenoid valve. The cooling channel is arranged in the interlayer of the barrel wall of the beating barrel and is spiral around the center of the beating barrel. The coolant inlet pipe is communicated with one end of the cooling channel, the coolant outlet pipe is communicated with the other end of the cooling channel, and the cooling solenoid valve is arranged on the coolant inlet pipe.
6. The automatic pulp beater according to claim 5, characterized in that, The cooling medium in the cooling device is ethylene glycol.
7. The automatic pulp beater according to claim 5, characterized in that, The beating barrel is provided with a temperature sensor.
8. The automatic pulp beater according to claim 7, characterized in that, The bottom of the beating barrel is wedge-shaped, and a pulp outlet is provided at the lowest part of the bottom of the beating barrel. The temperature sensor is arranged at the pulp outlet.
9. The automatic pulp beater according to claim 8, characterized in that, The beating barrel is connected with a pulp conveying device, which includes a pulp conveying pipe connected to the pulp outlet and a pulp conveying pump arranged on the pulp conveying pipe.
10. The automatic pulp beater according to claim 1, characterized in that, An on-line viscometer is arranged at the bottom of the beating barrel.