Pulping control method and device, storage medium and food processor

Abstract

The invention provides a pulping control method and device, a storage medium and a food processer, the method is applied to the field of cooking, and the method comprises the following steps: in response to a cooking execution instruction, entering an oxygen discharging stage, and creating a weakly acidic and oxygen-free environment through low-speed stirring while heating; then the water-material mixture is coarsely crushed, cage damage of nutrient substances is completed, then the water-material mixture enters a solid matter precipitation stage, a heating device is controlled through a second heating parameter to maintain the temperature of a third water-material mixture at a first temperature, the third water-material mixture is stirred slowly, solid matter in the material is promoted to be precipitated in a weak-acid and oxygen-deficient environment, the oxidation effect is reduced, and the solid matter precipitation stage is started; oxidation loss of protein and fat is reduced, meanwhile, fishy smell substances are reduced, soluble solids of a finished product are increased, then protein factor inactivation and material softening are completed through fine stewing and slow cooking in the slow boiling and concentration process, smashing is completed in a high-temperature environment in the emulsifying and pulping stage, and fusion of nutrient substances is promoted; and the grease is fully emulsified.

Description

Technical Field

[0001] This application relates to the field of cooking, and more specifically, to a method, apparatus, storage medium, and food processor for controlling the preparation of food. Background Technology

[0002] As a major consumer of legumes, China has a long history of producing soy milk, a plant-based protein beverage. With the advent of small appliances like soy milk makers, homemade soy milk has become incredibly popular. Current soy milk makers primarily focus on two common grinding processes: raw grinding and cooked grinding. Raw grinding mimics traditional stone grinding, first crushing and grinding the soybeans before boiling to deactivate enzymes. However, during this process, the release of lipoxygenase (LOX) and peroxidase (POD) from the ground soybeans can induce fatty acid oxidation, producing beany-smelling substances that negatively impact the quality of the soy milk. Cooked grinding, another commonly used grinding technique in soy milk makers, effectively reduces the beany taste in the final product, but its protein and other nutritional solids content are far less than that of raw grinding. Therefore, finding a soy milk cooking technique that can both reduce the beany taste and maximize nutrient retention remains to be explored. Summary of the Invention

[0003] This application provides a pulping control method, apparatus, storage medium, and food processor. The method can ensure that the soluble solids, i.e. nutrients, of the pulp are increased and the taste of the pulp is improved.

[0004] In a first aspect, a pulping control method is provided, applied to a food processor, the food processor including a stirring device and a heating device. The method includes: in response to a cooking execution command, when the food processor enters an oxygen removal stage, controlling the heating device to heat a first water-material mixture in the cooking chamber of the food processor according to a first heating parameter, and controlling the stirring device to stir the first water-material mixture according to a first stirring parameter to obtain a second water-material mixture; when the food processor enters a coarse grinding stage, controlling the stirring device to grind the second water-material mixture according to a second stirring parameter to obtain a third water-material mixture; wherein the average particle size of the material particles in the third water-material mixture is less than [a certain value]. The average particle size of the material particles in the second water-material mixture; when the food processor enters the solid precipitation stage, the heating device is controlled according to the second heating parameter to maintain the temperature of the third water-material mixture at the first temperature, and the stirring device is controlled according to the third stirring parameter to stir the third water-material mixture to obtain the fourth water-material mixture; when the food processor enters the slow boiling and thickening stage, the heating device is controlled according to the third heating parameter to heat the fourth water-material mixture to obtain the fifth water-material mixture; when the food processor enters the emulsification and pulping stage, the stirring device is controlled according to the fourth stirring parameter to pulverize the fifth water-material mixture to form a slurry.

[0005] Through the above technical solution, in the pulping process of the food processor, the food processor first enters the oxygen removal stage. By heating and stirring at low speed, the stirring process controlled by the first stirring parameter does not break the pulp material. Instead, the stirring promotes the removal of oxygen from the water during the heating process and increases the concentration of ionized hydrogen ions, thereby lowering the pH and creating a weakly acidic, low-oxygen environment, which allows the seed coat of the pulp material to fully absorb water and expand. The water-material mixture is then coarsely pulverized to reduce the particle size of the pulping material, thus breaking down the nutrient cage. However, the pulping material is not completely ground to a fluid particle size, at which point fat oxidase is less likely to act, effectively reducing the fishy smell caused by fat oxidation. Next, the solids precipitation stage begins. The heating device is controlled by the second heating parameter to maintain the temperature of the third water-material mixture at the first temperature, and it is stirred by the third stirring parameter to promote the precipitation of solids in the material in a weakly acidic and low-oxygen environment, reducing oxidation. While reducing the oxidation loss of protein and fat, it ensures that the fishy smell is reduced and the soluble solids of the finished product are increased. Then, in the slow boiling and concentration process, the anti-protein factor is inactivated and the material is softened. Finally, in the emulsification pulping stage, the pulverization is completed at high temperature, promoting the fusion of nutrients and fully emulsifying the oil, thus producing a pulp rich in nutrients, low in unpleasant flavor substances, and with a good taste.

[0006] In conjunction with the first aspect, in some possible implementations, the food processor further includes a water injection device. In response to a cooking execution command, when the food processor enters the deoxygenation stage, the heating device is controlled according to a first heating parameter to heat the first water-material mixture in the cooking chamber of the food processor, and the stirring device is controlled according to a first stirring parameter to stir the first water-material mixture to obtain a second water-material mixture. This includes: in response to the cooking execution command, determining a set pulping amount corresponding to the cooking execution command; controlling the water injection device to inject water into the cooking chamber of the food processor according to the set pulping amount; after detecting that the water volume in the cooking chamber meets the set pulping amount, determining that the food processor has entered the deoxygenation stage, controlling the heating device according to the first heating parameter to heat the first water-material mixture in the cooking chamber of the food processor, and controlling the stirring device according to the first stirring parameter to stir the first water-material mixture to obtain a second water-material mixture.

[0007] In combination with the first aspect and the above implementation, in some possible implementations, controlling the heating device to heat the first water-material mixture in the cooking cavity of the food processor according to the first heating parameter includes: controlling the heating device to heat the first water-material mixture in the cooking cavity of the food processor with a first heating power until the temperature of the first water-material mixture reaches a second temperature.

[0008] Combining the first aspect and the above implementation methods, in some possible implementation methods, the first heating power P1 satisfies that P1 is greater than or equal to 1000W and less than or equal to 1200W, and the second temperature T1 satisfies that it is greater than or equal to 78℃ and less than or equal to 82℃.

[0009] In combination with the first aspect and the above implementation, in some possible implementations, controlling the stirring device to stir the first water-material mixture according to the first stirring parameter includes: controlling the stirring device to stir the first water-material mixture at a first stirring speed.

[0010] In combination with the first aspect and the above implementation, in some possible implementations, the control stirring device stirs the first water-material mixture at a first stirring speed, including: at each first preset interval, the control stirring device stirs the first water-material mixture at the first stirring speed, and the stirring time is the first stirring time.

[0011] Combining the first aspect and the above implementation methods, in some possible implementation methods, the first stirring speed is the minimum speed allowed by the stirring device motor.

[0012] Combining the first aspect and the above implementation methods, in some possible implementation methods, the minimum allowable speed of the motor is greater than 1000 r / min and less than 3000 r / min.

[0013] Combining the first aspect and the above implementation methods, in some possible implementation methods, the first preset interval duration t1 satisfies t1 greater than or equal to 50s and less than or equal to 70s, and the first stirring duration t2 satisfies t2 greater than 0s and less than or equal to 6s.

[0014] In combination with the first aspect and the above implementation, in some possible implementations, when the food processor enters the coarse grinding stage, the mixing device is controlled to grind the second water-material mixture according to the second mixing parameters to obtain the third water-material mixture, including: when the food processor enters the coarse grinding stage, the mixing device is controlled to grind the second water-material mixture at a second mixing speed, and the mixing time is the second mixing time, so as to obtain the third water-material mixture.

[0015] Combining the first aspect and the above implementation methods, in some possible implementation methods, the second stirring speed r2 satisfies that r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and the second stirring duration t3 is greater than or equal to 0.5 min and less than or equal to 1.5 min.

[0016] In combination with the first aspect and the above implementation, in some possible implementations, when the food processor enters the solids precipitation stage, controlling the heating device to maintain the temperature of the third water-material mixture at the first temperature according to the second heating parameter includes: when the food processor enters the solids precipitation stage, controlling the heating device to heat the third water-material mixture in the cooking cavity of the food processor with the second heating power so that the temperature of the third water-material mixture is maintained at the first temperature.

[0017] In combination with the first aspect and the above implementation, in some possible implementations, controlling the stirring device to stir the third water-material mixture according to the third stirring parameters includes: controlling the stirring device to stir the third water-material mixture at a third stirring speed.

[0018] In combination with the first aspect and the above implementation, in some possible implementations, the control stirring device stirs the third water-material mixture at a third stirring speed, including: every second preset interval, the control stirring device stirs the third water-material mixture at a third stirring speed, and the stirring time is the third stirring time.

[0019] Combining the first aspect and the above implementation methods, in some possible implementation methods, the second preset interval duration t4 satisfies t4 greater than or equal to 25s and less than or equal to 35s, the third stirring speed r3 satisfies r3 greater than 1000r / min and less than 3000r / min, and the third stirring duration t5 satisfies t5 greater than 0s and less than or equal to 6s.

[0020] In combination with the first aspect and the above implementation, in some possible implementations, when the food processor enters the slow boiling and thickening stage, the heating device is controlled according to the third heating parameter to heat the fourth water-material mixture in the cooking cavity of the food processor to obtain the fifth water-material mixture, including: after the maintenance time of the first temperature reaches the first preset duration, it is determined that the food processor has entered the slow boiling and thickening stage, and the heating device is controlled according to the third heating parameter to heat the fourth water-material mixture in the cooking cavity of the food processor to obtain the fifth water-material mixture.

[0021] In combination with the first aspect and the above implementation, in some possible implementations, when the food processor enters the slow boiling and thickening stage, the heating device is controlled to heat the fourth water mixture according to the third heating parameter to obtain the fifth water mixture. This includes: when the food processor enters the slow boiling and thickening stage, the heating device is controlled to heat the fourth water mixture at a preset heating rate until the temperature of the fourth water mixture reaches the third temperature to obtain the fifth water mixture.

[0022] Combining the first aspect and the above implementation methods, in some possible implementation methods, the preset heating rate K satisfies that K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min.

[0023] In combination with the first aspect and the above implementation, in some possible implementations, when the food processor enters the emulsification and pulping stage, the stirring device is controlled to pulverize the fifth water-material mixture according to the fourth stirring parameter so that the fifth water-material mixture forms a slurry, including: after the third temperature is maintained for a second preset time, it is determined that the food processor has entered the emulsification and pulping stage, and the stirring device is controlled to pulverize the fifth water-material mixture according to the fourth stirring parameter so that the fifth water-material mixture forms a slurry.

[0024] In combination with the first aspect and the above implementation, in some possible implementations, controlling the stirring device to crush the fifth water-material mixture according to the fourth stirring parameter to form a slurry includes: controlling the stirring device to crush the fifth water-material mixture at a fourth stirring speed at every third preset interval, the stirring time being the fourth stirring time, until the cumulative stirring time reaches the fifth stirring time.

[0025] Combining the first aspect and the above implementation methods, in some possible implementation methods, the fourth stirring speed r4 satisfies that r4 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min, and the fifth stirring duration t6 satisfies that t6 is greater than or equal to 15 min and less than or equal to 25 min.

[0026] In combination with the first aspect and the above implementation, in some possible implementations, the method further includes: detecting the temperature of the fifth water-material mixture during each third interval; when the temperature is lower than the fourth temperature, controlling the heating device to heat the fifth water-material mixture according to the fourth heating parameter so that the temperature of the fifth water-material mixture reaches the fourth temperature.

[0027] In combination with the first aspect and the above implementation, in some possible implementations, when the temperature is lower than the fourth temperature, controlling the heating device to heat the fifth water-material mixture according to the fourth heating parameter so that the temperature of the fifth water-material mixture reaches the fourth temperature includes: when the temperature is lower than the fourth temperature, controlling the heating device to heat the fourth water-material mixture with a third heating power until the temperature of the fourth water-material mixture reaches the fourth temperature.

[0028] Secondly, a pulping control method is provided for use in a food processor, the method comprising:

[0029] Aeration stage: The water-material mixture is heated to temperature T1 with heating power P1, wherein T1 is greater than or equal to 78℃ and less than or equal to 82℃, P1 is greater than or equal to 1000w and less than or equal to 1200w, and the water-material mixture is stirred without pulverization at a first stirring speed r1 and a first stirring time at a first preset interval, wherein r1 is greater than or equal to 1000r / min and less than or equal to 3000r / min;

[0030] Coarse crushing stage: After the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min.

[0031] Slow boiling enrichment stage: Heat to the third temperature T2 = T boiling point - 5℃ at an average heating rate K, where K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min;

[0032] Emulsification and pulping stage: After the slow boiling and thickening stage is completed, the mixture is intermittently stirred at a stirring speed of r3, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is followed by a second preset interval, and the cumulative stirring time is t3, which is greater than or equal to 15 min and less than or equal to 25 min.

[0033] Thirdly, a pulping control method is provided for use in a food processor, the method comprising:

[0034] Coarse crushing stage: After the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min.

[0035] Solid precipitation stage: After the coarse crushing stage is completed, maintain the constant temperature T1 for a preset time of 10min≤t1≤20min. During the constant temperature period, stir the water-material mixture at a stirring speed of 1000r / min≤r1≤3000r / min every first preset interval.

[0036] Slow boiling enrichment stage: Heat to the third temperature T2 = T boiling point - 5℃ at an average heating rate K, where K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min;

[0037] Emulsification and pulping stage: After the slow boiling and thickening stage is completed, the mixture is intermittently stirred at a stirring speed of r3, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is followed by a second preset interval, and the cumulative stirring time is t3, which is greater than or equal to 15 min and less than or equal to 25 min.

[0038] Fourthly, a pulping control method is provided for use in a food processor, the method comprising:

[0039] Aeration stage: The water-material mixture is heated to temperature T1 with heating power P1, wherein T1 is greater than or equal to 78℃ and less than or equal to 82℃, P1 is greater than or equal to 1000w and less than or equal to 1200w, and the water-material mixture is stirred without pulverization at a first stirring speed r1 and a first stirring time at a first preset interval, wherein r1 is greater than or equal to 1000r / min and less than or equal to 3000r / min;

[0040] Coarse crushing stage: After the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min.

[0041] Solid precipitation stage: After the coarse crushing stage is completed, maintain the constant temperature T1 for a preset time of 10min≤t4≤20min. During the constant temperature period, stir the water-material mixture at a stirring speed of 1000r / min≤r4≤3000r / min every third preset interval.

[0042] Emulsification and pulping stage: Heat to T2, where T2 is greater than T1, and intermittently stir at a stirring speed r, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is followed by a second preset interval, and the cumulative stirring time is t3, which is greater than or equal to 15 min and less than or equal to 25 min.

[0043] Fifthly, a pulping control method is provided for use in a food processor, the method comprising:

[0044] Coarse crushing stage: After the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min.

[0045] Solid precipitation stage: After the coarse crushing stage is completed, maintain the constant temperature T1 for a preset time of 10min≤t1≤20min. During the constant temperature period, stir the water-material mixture at a stirring speed of 1000r / min≤r1≤3000r / min every first preset interval.

[0046] Slow boiling enrichment stage: Heat to the third temperature T2 = T boiling point - 5℃ at an average heating rate K, where K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min;

[0047] Emulsification and pulping stage: After the slow boiling and thickening stage is completed, the mixture is intermittently stirred at a stirring speed r3, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is followed by a second preset interval, and the cumulative stirring time is t3. t3 is greater than or equal to 15 min and less than or equal to 25 min. The temperature of the water-material mixture is detected within each second preset interval. When the temperature is lower than T3, heating power P2 is used to supplement the heat.

[0048] Sixthly, a pulping control device is provided, the device comprising:

[0049] The first control unit is used to respond to the cooking execution command. When the food processor enters the oxygen removal stage, it controls the heating device to heat the first water-material mixture in the cooking chamber of the food processor according to the first heating parameters, and controls the stirring device to stir the first water-material mixture according to the first stirring parameters to obtain the second water-material mixture.

[0050] The second control unit is used to control the mixing device to crush the second water-material mixture according to the second mixing parameters when the food processor enters the coarse crushing stage, so as to obtain the third water-material mixture; the average particle size of the material particles in the third water-material mixture is smaller than the average particle size of the material particles in the second water-material mixture.

[0051] The third control unit is used to control the heating device to maintain the temperature of the third water-material mixture at the first temperature according to the second heating parameters when the food processor enters the solids precipitation stage, and to control the stirring device to stir the third water-material mixture according to the third stirring parameters to obtain the fourth water-material mixture.

[0052] The fourth control unit is used to control the heating device to heat the fourth water mixture according to the third heating parameters when the food processor enters the slow boiling and thickening stage, so as to obtain the fifth water mixture.

[0053] The fifth control unit is used to control the mixing device to crush the fifth water-material mixture according to the fourth mixing parameters when the food processor enters the emulsification and pulping stage, so as to form a slurry from the fifth water-material mixture.

[0054] In a seventh aspect, a food processor is provided, the food processor including: a memory for storing executable program code;

[0055] A processor for calling and running executable program code from memory to perform the methods in the first aspect or any possible implementation of the first aspect described above.

[0056] Eighthly, a computer program product is provided, comprising: computer program code, which, when run on a computer, causes the computer to perform the methods described in the first aspect or any possible implementation thereof.

[0057] Ninthly, a computer-readable storage medium is provided that stores computer program code, which, when executed on a computer, causes the computer to perform the methods described in the first aspect or any possible implementation thereof. Attached Figure Description

[0058] Figure 1 This is a schematic diagram of the structure of a food processor in one embodiment of this application;

[0059] Figure 2 This is a partial structural schematic diagram of a food processor in one embodiment of this application;

[0060] Figure 3 This is a schematic flowchart of a pulping control method provided in an embodiment of this application;

[0061] Figure 4 This is a schematic flowchart of a pulping control method provided in an embodiment of this application;

[0062] Figure 5 This is a schematic flowchart of a pulping control method provided in an embodiment of this application;

[0063] Figure 6 This is a schematic diagram of the overall process of a pulping control method provided in an embodiment of this application;

[0064] Figure 7 This is a schematic flowchart of a pulping control method provided in an embodiment of this application;

[0065] Figure 8 This is a schematic flowchart of a pulping control method provided in an embodiment of this application;

[0066] Figure 9 This is a schematic flowchart of a pulping control method provided in an embodiment of this application;

[0067] Figure 10 This is a schematic flowchart of a pulping control method provided in an embodiment of this application;

[0068] Figure 11 This is a schematic diagram of the structure of a pulping control device provided in an embodiment of this application;

[0069] Figure 12 This is a schematic diagram of the structure of a pulping control device provided in an embodiment of this application;

[0070] Figure 13 This is a schematic diagram of the structure of a pulping control device provided in an embodiment of this application;

[0071] Figure 14 This is a schematic diagram of the structure of a pulping control device provided in an embodiment of this application;

[0072] Figure 15 This is a schematic diagram of the structure of a pulping control device provided in an embodiment of this application;

[0073] Figure 16 This is a schematic diagram of the structure of a food processor provided in an embodiment of this application.

[0074] Explanation of reference numerals in the attached diagram: 1. Food processor; 2. Noise shield; 3. Cup assembly; 4. Lower base; 5. Water inlet assembly. Detailed Implementation

[0075] The technical solutions in this application will be clearly and thoroughly described below with reference to the accompanying drawings. In the description of the embodiments of this application, unless otherwise stated, " / " means "or," for example, A / B can mean A or B. "And / or" in the text is merely a description of the relationship between related objects, indicating that three relationships can exist. For example, A and / or B can represent: A existing alone, A and B existing simultaneously, and B existing alone. Furthermore, in the description of the embodiments of this application, "multiple" refers to two or more than two.

[0076] Hereinafter, the terms "first" and "second" are used for descriptive purposes only and should not be construed as implying or suggesting relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature.

[0077] To make the objectives, technical solutions, and advantages of this application clearer, the following detailed description is provided in conjunction with the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative and not intended to limit the scope of this application.

[0078] Please refer to Figure 1 This application provides a food processor 1, which includes a soundproof cover 2, a cup assembly 3, a lower base 4, and a water injection assembly 4.

[0079] The cup assembly 3 includes a cup body, a handle, a heating device, and a stirring device. A lid assembly (not labeled) covers the cup body and cooperates with it to form a cooking cavity. The cup body is used to hold ingredients (e.g., water and / or pulping materials). The heating device is used to heat the ingredients within the cooking cavity. The heating method of the heating device can be at least one of resistance heating, infrared heating, and electromagnetic heating. In other embodiments, the heating device can also employ other heating methods. In this application embodiment, the specific heating method of the heating device is not limited. It is understood that the heating device can be installed at least at the bottom of the cup body and around the perimeter of the cup body. Optionally, the cup body can be provided with a recessed depth to form a recessed compartment, and the heating device can be installed around the recessed compartment of the cup body to uniformly heat the ingredients within the recessed compartment. Optionally, a temperature sensor is provided at the bottom of the cup body to detect the temperature of the ingredients within the cooking cavity.

[0080] For example, when the heating device includes a resistance heating wire, the resistance heating wire can be arranged around the bottom of the cup body, and the two ends of the resistance heating wire are respectively connected to the positive and negative terminals of the power supply. At this time, the area near the two ends of the resistance heating wire is the cold end area, and the rest is the hot end area.

[0081] The stirring device is used to stir or pulverize ingredients within the cooking cavity to suit the user's eating needs. It is understood that the stirring device is detachably mounted at the bottom of the cooking cavity, allowing the user to choose whether to place the stirring device within the food processor 1 based on the specific food being prepared. Furthermore, the food processor 1 can be equipped with multiple stirring devices, allowing the user to conveniently select different devices to prepare different foods depending on the ingredients. It is understood that the stirring device includes at least one stirring blade; exemplaryly, the stirring device may include two, three, or four stirring blades for stirring or pulverizing ingredients within the cooking cavity.

[0082] The main unit (not shown in the figure) can be installed in the lower base 4. The main unit is connected to and electrically connected to the cup assembly 3. The main unit can be connected to a power source to supply power to the cup assembly 3. The main unit includes a motor (not shown in the figure) and a controller (not shown in the figure). The motor is connected to the controller, and the output shaft of the motor can be connected to a stirring device to drive the stirring device to rotate, thereby stirring or crushing the food in the cooking cavity. The controller can be connected to a heating device to control the start and stop of the heating device and the heating power to adapt to the food preparation program. The controller can also be connected to a temperature sensor to control the temperature sensor to obtain the temperature of the food in the cooking cavity.

[0083] Understandably, the main unit can be detachably connected to the bottom of the cup assembly 3. Compared to a design where the main unit 3 and cup assembly 3 are not detachable, the cup assembly 3 can be removed from the main unit when cleaning is required. This prevents water from entering the main unit, reducing the probability of damage and extending its lifespan. Consequently, the food processor 1 also has a longer lifespan. Furthermore, cleaning the cup assembly 3 separately, compared to cleaning the main unit and cup assembly 3 together, reduces the weight in the user's hand, thus improving the convenience of cleaning the cup assembly 3.

[0084] Understandably, since the main unit 3 can be detachably connected to the cup body component 3, if either the main unit or the cup body component 3 is damaged, either the main unit or the cup body component 3 can be replaced or repaired separately, thereby improving the convenience of maintenance and reducing the user's maintenance costs.

[0085] The cup lid assembly 4 can be placed over the opening of the cup body to seal the opening and prevent food from splashing out of the cooking chamber through the opening. This can prevent food waste and reduce the probability of food contaminating the outer surface of the food processor 1 or the countertop where the food processor 1 is placed, thereby improving the user's cleaning convenience and user experience.

[0086] Please see Figure 2 This is a partial structural diagram of a food processor in one embodiment of this application. Figure 2 The water filling structure in the lower base 4 is described. The lower base 4 includes a housing, a water pump, and a water delivery pipe, with the water pump and water delivery pipe housed within the housing. The water filling assembly 5 includes a water tank on the left side. The controller can control the water filling assembly to draw water from the lower part of the left water tank using the water pump, deliver it through the water delivery pipe to the water inlet at the bottom of the right cup body, and then discharge water from the outlet in the handle of the cup body assembly 3, completing the water filling process.

[0087] It should be noted that the above illustration is only one embodiment of the food processor. In other embodiments, the food processor may not include a water injection device, and water may be manually injected into the cooking cavity.

[0088] like Figure 1-2 As shown, the pulping control method provided in this application embodiment can be applied to the pulping process of a food processor. The food processor 1 includes, but is not limited to, a high-speed blender and a soymilk maker. The pulping material can be one or more of the following: grains, cereals, etc. For example, the pulping material can be one or more of the following: sorghum, buckwheat, oats, broad beans, black beans, soybeans, etc. The food processor includes a stirring device and a heating device. Optionally, the food processor may also include a water injection device. In response to cooking execution commands, when the food processor enters the oxygen removal stage, it controls the heating device to heat the first water-material mixture in the cooking chamber according to the first heating parameters, and controls the stirring device to stir the first water-material mixture according to the first stirring parameters to obtain a second water-material mixture. When the food processor enters the coarse grinding stage, it controls the stirring device to grind the second water-material mixture according to the second stirring parameters to obtain a third water-material mixture. When the food processor enters the solid precipitation stage, it controls the heating device to maintain the temperature of the third water-material mixture at a first temperature according to the second heating parameters, and controls the stirring device to stir the third water-material mixture according to the third stirring parameters to obtain a fourth water-material mixture. When the food processor enters the slow boiling and thickening stage, it controls the heating device to heat the fourth water-material mixture according to the third heating parameters to obtain a fifth water-material mixture. When the food processor enters the emulsification and pulping stage, it controls the stirring device to grind the fifth water-material mixture according to the fourth stirring parameters to form a slurry.

[0089] based on Figure 1-2 The food processor shown below will be combined with... Figures 3-6 The pulping control method provided in the embodiments of this application will be described in detail.

[0090] Please see Figure 3 , Figure 3 This is a schematic flowchart of a pulping control method provided in an embodiment of this application. Figure 3 As shown, the method in this application embodiment may include the following steps S101-S105.

[0091] S101, in response to the cooking execution command, when the food processor enters the oxygen removal stage, the heating device is controlled to heat the first water-material mixture in the cooking chamber of the food processor according to the first heating parameter, and the stirring device is controlled to stir the first water-material mixture according to the first stirring parameter to obtain the second water-material mixture;

[0092] In one embodiment, the food processor includes a mixing device and a heating device. The mixing device can be used to mix or grind food to improve the texture of the final slurry. The heating device is used to provide heat to the food processor.

[0093] Specifically, the raw materials and an appropriate amount of water are placed into the blending cup of the food processor, and the cup is closed. The cooking execution command is the command to control the food processor to start cooking. The cooking execution command can be triggered by the user through the start blending button set in the food processor, or it can be triggered by other terminal devices connected to the food processor. For example, a control program for controlling the food processor can be installed on a mobile phone connected to the food processor. When the user clicks the start blending button in the operation interface of the control program, a cooking command is sent to the food processor. In this embodiment, the cooking execution command is triggered when the user selects the concentrated soy milk mode. In the concentrated soy milk mode, the soy milk produced by the food processor has a higher soluble solids content, that is, a higher protein and fat content, resulting in a richer and thicker taste. It is understood that this blending control method can also be used to cook mixed grain paste, corn juice, etc., to improve the taste of the resulting liquid and the nutrients it contains.

[0094] When the food processor receives a cooking execution command, it determines the first heating parameters for the oxygen removal stage according to the preset cooking program. Based on these parameters, it controls the heating device to heat the first water-material mixture, and simultaneously controls the stirring device to stir the mixture while heating, based on the first stirring parameters. The water-material mixture after the oxygen removal stage is referred to as the second water-material mixture. The stirring device can be intermittent or continuous. The stirring device uses an ultra-low speed with no pulverizing effect to stir the first water-material mixture by controlling the rotation speed. Stirring promotes the removal of oxygen from the water during the heating process and increases the concentration of hydrogen ions ionized in the water, thus lowering the pH and creating a weakly acidic, low-oxygen environment, allowing the seed coat of the pulping material to fully absorb water and expand.

[0095] It should be noted that soybeans contain enzymes that induce enzymatic oxidation reactions, producing certain unpleasant flavor compounds. Lipoxygenase (LOX) and peroxidase (POD) can induce fatty acid oxidative decomposition, which is the main cause of the beany taste. During roasting, POD is considered the most heat-resistant endogenous enzyme in legumes. Appropriate heat treatment can effectively deactivate the activity of endogenous oxidases, thereby inhibiting the formation of beany taste. To prevent the formation of beany compounds during cooking, the primary heating parameter can be selected based on the properties of the ingredients, and the food can be cooked at a specific temperature. For example, a water-ingredient mixture can be heated to above 50°C. At this temperature, lipoxygenase is less likely to activate, thus inhibiting the formation of unpleasant flavor compounds during cooking. However, the temperature should not be too high, as excessively high temperatures may cause denaturation of solids such as proteins, preventing them from dissolving. Therefore, the temperature can be set between 78°C and 82°C.

[0096] S102, when the food processor enters the coarse grinding stage, the mixing device is controlled to grind the second water-material mixture according to the second mixing parameters to obtain the third water-material mixture;

[0097] In one embodiment, when the food processor enters the coarse grinding stage, the stirring device is controlled to grind the second water-material mixture, thereby reducing the average particle size of the material particles in the second water-material mixture. After the coarse grinding stage, the average particle size of the material particles in the third water-material mixture is smaller than that of the material particles in the second water-material mixture. It should be noted that the material particles may be regularly shaped, such as nearly spherical granules, or they may be irregularly shaped, such as lumps, and there is no specific limitation. The material particles in the third water-material mixture are irregularly shaped after the material particles have been crushed. It is understood that if the pulping material is ground too finely, it will promote the release of lipoxygenase, which will produce fishy-smelling substances. Therefore, the average particle size of the material particles in the third water-material mixture cannot reach the fluid particle size. For a more vivid description, the material particles in the third water-material mixture are medium-sized particles, such as small lumps. The particle size range of the fluid particles in the particulate two-phase flow system is 10. -5 ~10 - 2 Therefore, the average particle size of the material particles in the third water-material mixture should be greater than 10 cm. -5 ~10 -2 At the same time, it is smaller than the average diameter of the material particles in the second water-material mixture.

[0098] The second mixing parameter may include mixing time, mixing speed, mixing interval, etc., which can be set according to the added materials and food cooking requirements.

[0099] S103, when the food processor enters the solids precipitation stage, the heating device is controlled according to the second heating parameter to maintain the temperature of the third water mixture at the first temperature, and the stirring device is controlled according to the third stirring parameter to stir the third water mixture to obtain the fourth water mixture.

[0100] In one embodiment, after the food processor pulverizes the material particles for a period of time to obtain particles of the desired particle size, it enters the solids precipitation stage. At this time, the temperature of the third water-material mixture is maintained at a first temperature according to the second heating parameters, and the stirring device is controlled to stir the third water-material mixture at a low speed according to the third stirring parameters. This promotes the precipitation of solids in the material in a weakly acidic and low-oxygen environment, reduces oxidation, and ensures that the odorous substances are reduced while increasing the soluble solids of the finished product, thus reducing the oxidative loss of proteins and fats. It should be noted that in order to ensure the reduction of odorous substances (unpleasant flavor substances), the cooking temperature also needs to be considered during the solids precipitation stage. That is, the first temperature can be set according to the properties of the material, for example, it can be set at 78℃~82℃, at which temperature odorous substances are less likely to be generated.

[0101] S104, When the food processor enters the slow boiling and thickening stage, the heating device is controlled to heat the fourth water mixture according to the third heating parameter to obtain the fifth water mixture;

[0102] In one embodiment, after the solids in the food processor are separated, the process enters a slow boiling and concentration stage. The heating parameters are controlled by a third heating parameter to heat the fourth water-material mixture. During this process, slow simmering and cooking deactivates anti-nutritional factors and softens the materials. Anti-nutritional factors are substances that affect or inhibit the absorption of nutrients in food, such as anti-protein factors present in legumes, grains, and tubers. Since anti-protein factors have poor heat resistance, they can be eliminated through thorough heating. The third heating parameter can be set according to the temperature required to kill the anti-nutritional factors contained in the materials. Generally, a high temperature needs to be maintained during the slow boiling and concentration stage to inactivate released lipoxygenases and unreleased lipoxygenases present in small pieces of material, preventing the formation of a beany odor due to oxidation of fats by uninactivated lipoxygenases during subsequent processing, thus achieving the purpose of deodorization. On the other hand, slow boiling and concentration denatures and degrades the proteins dissolved from coarse grinding, producing more free amino acids, including umami amino acids, thus enhancing flavor. The fifth water-material mixture is the water-material mixture obtained by heating the fourth water-material mixture.

[0103] S105, when the food processor enters the emulsification and pulping stage, the mixing device is controlled to crush the fifth water-material mixture according to the fourth mixing parameter so that the fifth water-material mixture forms a slurry.

[0104] In one embodiment, when the food processor enters the emulsification and slurry-making stage, since the material has already been softened after coarse grinding in the slow boiling and thickening stage, it is easier to grind and emulsify the material, thus improving grinding efficiency. The fifth water-material mixture is ground by controlling the stirring device with the fourth stirring parameter. During this process, grinding is completed, promoting the fusion and precipitation of nutrients, and ensuring sufficient emulsification of the oil, so that the fifth water-material mixture forms a slurry. The stirring time can be at least 15 minutes; prolonged heating and grinding facilitates the formation of soluble solids and ensures thorough emulsification of the oil.

[0105] In this embodiment of the application, in response to the cooking execution command, the food processor first enters the oxygen removal stage. By heating and stirring at low speed, the pulping material is not broken. Stirring promotes the removal of oxygen from the water during the heating process and increases the concentration of ionized hydrogen ions, thereby lowering the pH and creating a weakly acidic, low-oxygen environment, which allows the seed coat of the pulping material to fully absorb water and expand. The water-material mixture is then coarsely pulverized to reduce the particle size of the pulping material, thus breaking down the nutrient cage. However, the pulping material is not completely ground to a fluid particle size, at which undesirable flavor substances are less likely to react, effectively reducing their formation. Next, the solids precipitation stage begins. The heating device is controlled by a second heating parameter to maintain the temperature of the third water-material mixture at the first temperature, and it is stirred by a third stirring parameter to promote the precipitation of solids in the material in a weakly acidic and low-oxygen environment, reducing oxidation. This reduces the oxidative loss of proteins and fats while minimizing fishy odors and increasing the soluble solids content of the finished product. Then, during the slow boiling and concentration process, the anti-protein factors are inactivated and the material is softened. Finally, the emulsification pulping stage is carried out at high temperature to complete the pulverization and promote the fusion of nutrients, and to fully emulsify the oils, thereby producing a slurry rich in nutrients, low in undesirable flavor substances, and with a good taste.

[0106] Please see Figure 4 , Figure 4 This is a schematic flowchart of a pulping control method provided in an embodiment of this application. Figure 4 As shown, the method in this application embodiment may include the following steps S201-S203.

[0107] S201, in response to the cooking execution command, determines the set pulping amount corresponding to the cooking execution command;

[0108] In one embodiment, in response to a cooking execution command, the user can set the amount of puree to be made. In one feasible implementation, after the user adds the puree material to the blending cup and closes the lid, the user generates a cooking execution command by selecting a pureeing mode or clicking "Start." The controller receives this cooking execution command and generates an instruction message to instruct the user to select the puree amount, thereby obtaining the user's selected puree amount. The function of selecting the puree amount can be provided to the user in the food processor operating area or in a food processor control application installed on a mobile device.

[0109] S202, according to the set pulping amount, the water injection device injects water into the cooking cavity of the food processor;

[0110] In one embodiment, the food processor includes a water injection device that can automatically deliver water from a pre-stored water tank containing an appropriate amount of drinking water or other water sources into the cooking chamber. The food processor controls the water injection device to automatically complete the water injection according to the set pulping volume.

[0111] Optionally, a water level sensor (such as an ultrasonic sensor, pressure sensor, or float switch) is installed in the water tank to monitor the water level in real time. Once the set pulping volume is obtained, the water level sensor collects the water volume in the tank. Logic is written in the microcontroller to compare the real-time water volume with the set pulping volume. If the water volume is greater than or equal to the set pulping volume, water injection is performed.

[0112] Optionally, in response to the cooking execution command, the set pulping volume and set pulping concentration are obtained. Then, the water volume in the water tank and the weight of the pulping material are obtained. The water volume in the water tank is checked to see if it meets the set pulping volume, and the weight of the pulping material is checked to see if it meets the material requirements.

[0113] In one feasible implementation, the water level in the tank can be displayed on a screen within the food processor, allowing the user to easily check the water level. Optionally, if the user does not wish to add water when the water level in the tank is lower than the set blending volume, they can reset the set blending volume. Water is then added into the cooking chamber of the food processor via a water injection device.

[0114] S203, after detecting that the water volume in the cooking cavity meets the set pulping volume, the food processor enters the oxygen removal stage. The heating device is controlled to heat the first water-material mixture in the cooking cavity of the food processor according to the first heating parameter, and the stirring device is controlled to stir the first water-material mixture according to the first stirring parameter to obtain the second water-material mixture.

[0115] In one embodiment, after water is added to the set pulping amount, the food processor enters the oxygen removal stage. The heating device is controlled to heat the first water-material mixture according to the first heating parameter, and the stirring device is controlled to stir without pulverizing according to the first stirring parameter. After the oxygen removal stage is completed, the second water-material mixture is obtained.

[0116] In the embodiments of this specification, in response to a cooking execution command, a set pulping amount corresponding to the cooking execution command is determined. Water is injected into the cooking chamber of the food processor using a water injection device based on the set pulping amount. Once the water level in the cooking chamber is detected to meet the set pulping amount, the food processor enters the oxygen removal stage. A heating device is controlled to heat the first water-material mixture in the cooking chamber according to a first heating parameter, and a stirring device is controlled to stir the first water-material mixture according to a first stirring parameter to obtain a second water-material mixture. By setting a water injection device, automatic water injection based on the set pulping amount can be achieved, thereby detecting when the water level meets the set pulping amount before entering the oxygen removal stage, improving the intelligence of the pulping process.

[0117] Please see Figure 5 , Figure 5 This is a schematic flowchart of a pulping control method provided in an embodiment of this application. Figure 5 As shown, the method in this application embodiment may include the following steps S301-S305.

[0118] S301, in response to the cooking execution command, when the food processor enters the oxygen removal stage, the heating device is controlled to heat the first water-material mixture in the cooking chamber of the food processor with a first heating power until the temperature of the first water-material mixture reaches a second temperature, and the stirring device is controlled to stir the first water-material mixture with a first stirring speed to obtain the second water-material mixture.

[0119] In one embodiment, the first heating parameters include a first heating power and a second temperature. When the food processor enters the deoxygenation stage, the first water-ingredient mixture is heated with the first heating power to bring the temperature of the first water-ingredient mixture to the second temperature. The duration of the deoxygenation stage can be the time required to heat the first water-ingredient mixture to the second temperature.

[0120] Furthermore, in one embodiment, the first heating power P1 is greater than or equal to 1000W and less than or equal to 1200W, and the second temperature T1 is greater than or equal to 78°C and less than or equal to 82°C. The first heating power can be the full power of the heating device. This setting allows the temperature of the first water-material mixture to quickly reach the second temperature. Since the formation of odor-causing substances generally accumulates gradually with increasing temperature, full-power heating can quickly bypass the temperature range where odor-causing substances are generated and reach the preset second temperature.

[0121] In one embodiment, the first stirring parameter is a first stirring speed. While heating the first water-material mixture, the mixture is stirred at the first stirring speed during the heating process in the heating device to promote the removal of oxygen during heating and the release of hydrogen ions from the water. The first stirring speed is a low speed, and the pulping material is not pulverized.

[0122] Furthermore, in one embodiment, the method further includes:

[0123] At each first preset interval, the stirring device is controlled to stir the first water-material mixture at a first stirring speed for a duration equal to the first stirring time. Specifically, heating reduces the solubility of oxygen in water, and intermittent stirring helps release the gas during heating, making it easier for dissolved oxygen to escape. At the same time, during heating, the thermal motion of water increases, and intermittent stirring helps to increase the movement of water molecules, thereby increasing the generation of hydrogen ions (H+).

[0124] Furthermore, in one embodiment, the first stirring speed is the minimum speed allowed by the stirring device motor. Specifically, the first stirring speed can be set to the minimum speed allowed by the stirring device motor. High-speed stirring may cause some bubble formation, leading to air entrainment and increasing the oxygen content. Low-speed stirring can increase the contact between molecules, thereby promoting the self-ionization reaction of water to some extent and helping to maintain a low oxygen content.

[0125] Furthermore, in one embodiment, the minimum permissible speed of the motor is greater than 1000 r / min and less than 3000 r / min.

[0126] Further, in one embodiment, the first preset interval duration t1 satisfies t1 greater than or equal to 50s and less than or equal to 70s, and the first stirring duration t2 satisfies t2 greater than 0s and less than or equal to 6s. Preferably, the first preset interval duration is 60s, and the first stirring duration is 3 to 5s.

[0127] S302, when the food processor enters the coarse grinding stage, the stirring device is controlled to grind the second water-material mixture at the second stirring speed for the second stirring time to obtain the third water-material mixture;

[0128] In one embodiment, the second stirring parameters include a second stirring speed and a second stirring duration. When the temperature of the first water-material mixture reaches a second temperature, it enters the coarse crushing stage. At this time, the stirring device is controlled to crush the second water-material mixture at the second stirring speed for the second stirring duration, until the third water-material mixture is formed. By setting the second stirring duration and the second stirring speed, the average particle size of the material particles in the third water-material mixture can be controlled, making it into small pieces.

[0129] Furthermore, in one embodiment, the second stirring speed r2 satisfies that r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, preferably 5000 r / min, and the second stirring time is greater than or equal to 0.5 min and less than or equal to 1.5 min. Testing has shown that stirring the second water-material mixture at 5000 r / min for 0.5 to 1.5 min yields material particles of a suitable size. At this particle size, solids in the material particles are more easily precipitated, and undesirable flavor substances are less likely to be released.

[0130] S303, when the food processor enters the solids precipitation stage, the heating device is controlled to heat the third water-material mixture in the cooking chamber of the food processor with the second heating power so that the temperature of the third water-material mixture is maintained at the first temperature, and the stirring device is controlled to stir the third water-material mixture with the third stirring speed to obtain the fourth water-material mixture.

[0131] In one embodiment, after coarse grinding, the food processor enters the solids precipitation stage, and the second heating parameters include a second heating power and a first temperature. The heating device is controlled to maintain the temperature of the third water-material mixture at the first temperature using the second heating power. The first temperature can be the same as the second temperature described above, that is, the first temperature can be greater than or equal to 78°C and less than or equal to 82°C.

[0132] In one embodiment, the third stirring parameter is a third stirring speed. During the solid precipitation stage, while maintaining the first temperature, the third aqueous mixture is stirred at the third stirring speed to obtain a fourth aqueous mixture. The third stirring speed is also an ultra-low speed. Stirring at the third stirring speed at the second temperature helps to promote the precipitation of solids in a weakly acidic and low-oxygen environment, reducing oxidation. Furthermore, at this temperature, it can reduce the oxidative loss of proteins and fats while ensuring a reduction in fishy odor substances and increasing the soluble solids content of the finished product.

[0133] Furthermore, in one embodiment, at every second preset interval, the stirring device is controlled to stir the third water-material mixture at a third stirring speed, and the stirring time is the third stirring time. Specifically, the third stirring parameters include the third stirring speed, the second preset interval, and the third stirring time.

[0134] Further, in one embodiment, the second preset interval t4 satisfies t4 greater than or equal to 25s and less than or equal to 35s, the third stirring speed r3 satisfies r3 greater than 1000r / min and less than 3000r / min, and the third stirring duration t5 satisfies t5 greater than 0s and less than or equal to 6s. Preferably, the second preset interval is 30s, and the third stirring duration is 3-5s. Specifically, using intermittent stirring can avoid the introduction of oxygen due to excessive stirring. This setting can maximize the solids content in the liquid while minimizing the formation of undesirable flavor substances.

[0135] S304, after the first temperature is maintained for a first preset duration, the food processor is determined to enter the slow boiling and thickening stage. The heating device is controlled according to the third heating parameter to heat the fourth water-material mixture in the cooking chamber of the food processor to obtain the fifth water-material mixture.

[0136] In one embodiment, the duration of the solid precipitation stage is a first preset duration, which means that the temperature of the third water-material mixture is maintained at the first temperature and stirred for the first preset duration, after which the slow boiling concentration stage begins.

[0137] Furthermore, in one embodiment, when the food processor enters the slow boiling and thickening stage, the heating device is controlled to heat the fourth water-ingredient mixture at a preset heating rate until the temperature of the fourth water-ingredient mixture reaches the third temperature, so as to obtain the fifth water-ingredient mixture.

[0138] Specifically, in the slow-boiling enrichment stage, the third heating parameters include a preset heating rate and a third temperature. The heating device is controlled to slowly heat the mixture according to the preset heating rate until the temperature of the fourth water-material mixture reaches the third temperature, resulting in the fifth water-material mixture. The third temperature is close to the boiling point, for example, it could be the boiling point temperature minus 5°C. The main purpose of this slow-boiling enrichment stage is to cook the material, therefore the third temperature can be close to the boiling point temperature. By setting a preset heating rate, the rate at which the slurry heats up can be controlled. Heating at a slower rate makes it less likely for the liquid to boil violently, and the slower heating process ensures complete inactivation, reducing damage to proteins and thus improving its quality and edibility.

[0139] Furthermore, in one embodiment, the preset heating rate K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min.

[0140] S305, after the third temperature is maintained for the second preset time, the food processor is determined to enter the emulsification and pulping stage. The mixing device is controlled to crush the fifth water-material mixture according to the fourth mixing parameters so that the fifth water-material mixture forms a slurry.

[0141] In one embodiment, the third temperature is a temperature close to boiling. To prevent false boiling, after the third temperature is maintained for a second preset duration, it is determined that the fifth water-material mixture has reached the boiling temperature. The food processor is then determined to enter the emulsification and pulping stage. The stirring device is controlled to pulverize the fifth water-material mixture according to the fourth stirring parameters. Pulverization is carried out under high temperature to complete emulsification and pulping to achieve a delicate texture, so that the fifth water-material mixture forms a slurry.

[0142] Furthermore, in one embodiment, the stirring device is controlled to pulverize the fifth water-material mixture at a fourth stirring speed every third preset interval, and the stirring time is the fourth stirring time, until the cumulative stirring time reaches the fifth stirring time.

[0143] Specifically, the fourth stirring parameters include a third preset interval duration, a fourth stirring duration, and a fifth stirring duration. The fifth stirring duration is the total cumulative stirring time, and the fourth stirring duration is the duration of a single stirring cycle. The fourth stirring speed is selected as a high speed that can thoroughly grind the material while shortening the processing time. Simultaneously, by setting the third preset interval duration, the fifth water-material mixture is intermittently pulverized, which reduces the heat generated during pulverization, prevents overheating of small material pieces, thus preserving its nutritional components and flavor. It also ensures a more uniform pulverization process, avoiding situations where some parts are too fine while others remain coarse, ensuring a consistent final product texture, effectively improving the quality of the pulverization process, avoiding overheating and unevenness, and thus enhancing the taste of the slurry.

[0144] Furthermore, in one embodiment, the fourth stirring speed r4 satisfies that r4 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min, and the fifth stirring duration t6 satisfies that t6 is greater than or equal to 15 min and less than or equal to 25 min.

[0145] Specifically, the fourth stirring speed can be 10000 r / min. At this high speed, small pieces of material can be ground more thoroughly, resulting in a finer slurry texture. Furthermore, setting a stirring time of more than 15 minutes ensures thorough grinding of the small material pieces and also improves the pulverization effect. Preferably, the third preset interval can be 10 seconds, and the fourth stirring time can be 50 seconds.

[0146] Furthermore, in one embodiment, the method further includes: detecting the temperature of the fifth water-material mixture during each third interval; when the temperature is lower than the fourth temperature, controlling the heating device to heat the fifth water-material mixture according to the fourth heating parameter so that the temperature of the fifth water-material mixture reaches the fourth temperature.

[0147] Understandably, a suitable temperature facilitates the activity of oil molecules, making them more easily blended with water, thereby promoting full emulsification of the oil and improving the texture and taste of the soy milk. Therefore, the temperature of the fifth water-ingredient mixture is monitored during the grinding interval to ensure it does not fall below the fourth temperature due to heat loss. If it does fall below the fourth temperature, supplementary heating is applied using the fourth heating parameter, ensuring that the fifth water-ingredient mixture is ground and emulsified at a stable high temperature, improving overall processing efficiency and saving time and energy. The fourth temperature can be within a certain range lower than the third temperature; for example, the fourth temperature could be the third temperature -5℃; or, for instance, the fourth temperature could be the boiling point -10℃.

[0148] Further, in one embodiment, when the temperature is lower than the fourth temperature, controlling the heating device to heat the fifth water-material mixture according to the fourth heating parameter to bring the temperature of the fifth water-material mixture to the fourth temperature includes:

[0149] When the temperature is lower than the fourth temperature, the heating device is controlled to heat the fourth water-material mixture at the third heating power until the temperature of the fourth water-material mixture reaches the fourth temperature.

[0150] Specifically, the fourth heating parameters include a third heating power and a fourth temperature. When the temperature of the fifth water-material mixture is lower than the set fourth temperature, it is heated by the third heating power to bring the temperature of the fourth water-material mixture to the fourth temperature. After that, pulverization continues after the interval ends. For example, the third heating power can be 300-400W. Using lower power for supplemental heating can prevent scorching and boiling over.

[0151] Please see Figure 6 , Figure 6 This is a schematic diagram of the overall flow of a pulping control method provided in an embodiment of this application. Figure 6 As shown, in one embodiment, the pulping process can be specifically as follows: Select the concentrated soy milk mode to generate a cooking execution command, and then start cooking. First, enter the oxygen-removing and bean-awakening stage, heating to T1 (78℃≤T1≤82℃) at P1 (1000w≤P1≤1200w). During this process, every 1 minute, the motor performs ultra-low-speed stirring at r1 for 5 seconds without pulverization. This heating removes oxygen from the water and increases the concentration of ionized hydrogen ions, lowering the pH and creating a weakly acidic, low-oxygen environment. This allows the seed coat to fully absorb water and expand. r1 is the minimum speed the motor can reach (preferably less than 3000 r / min, greater than 1000 r / min). Then, enter the coarse pulverization stage. After reaching the set T1, the motor performs initial large-particle pulverization at a speed r2 (r2=5000 r / min) for t1 (0.5min≤t1≤1.5min). At this point, the material is in the state of medium-sized particles after crushing, completing the breaking down of the nutrient cage. Nutrients are released in a heat environment where fat oxidase is less active, effectively reducing the fishy smell caused by fat oxidation. The process then proceeds to the solids precipitation stage. After initial crushing, the temperature is maintained at T1 for a time t2 (10 min ≤ t2 ≤ 20 min). During this process, the mixture is stirred at an ultra-low speed (preferably less than 3000 r / min, greater than 1000 r / min) for 5 seconds every 30 seconds to promote the precipitation of solids in the material under a weakly acidic and low-oxygen environment, reducing oxidation. This minimizes the oxidative loss of protein and fat while reducing odorous substances and increasing the soluble solids content of the finished product. The process then proceeds to the slow boiling and concentration stage. After maintaining the temperature at T1 for a time t2, the mixture is heated to T2 at a heating efficiency K (1.2℃ / min ≤ K ≤ 2.0℃ / min). During this process, slow simmering completes the inactivation of anti-protein factors and softens the beans. Finally, the emulsification and pulping stage begins. After reaching T2 (T2 = boiling point - 5℃) and maintaining this temperature for at least 5 seconds, the mixture is further pulverized at high temperature to complete the emulsification and pulping process. During this process, the motor operates at a speed of r3 (r3 ≥ 10000 r / min) with intermittent stirring, stirring for 50 seconds, pausing for 10 seconds, and supplementing heating if the temperature drops below the boiling point by 10 degrees within the 10-second pause. The net stirring time throughout the entire process is greater than or equal to t2 (t2 ≥ 15 min). During the intermittent stirring, a heat power P2 (P2 = 300~400 W) is used to supplement heating and maintain the temperature. This process completes the pulverization and promotes the fusion of nutrients, ensuring thorough emulsification of the oils. It should be noted that, based on experiments, the soy milk prepared using the method described in the above examples can achieve a soluble solids content of 6.5% and a wet-basis protein content of 3.0%, which is double the effect compared to ordinary soy milk production.

[0152] In this embodiment, in response to a cooking execution command, when the food processor enters the deoxygenation stage, the heating device is controlled to heat the first water-material mixture in the cooking chamber of the food processor with a first heating power until the temperature of the first water-material mixture reaches a second temperature. The stirring device is then controlled to stir the first water-material mixture at a first stirring speed to obtain a second water-material mixture. When the food processor enters the coarse grinding stage, the stirring device is controlled to grind the second water-material mixture at a second stirring speed for a second stirring duration to obtain a third water-material mixture. When the food processor enters the solids precipitation stage, the heating device is controlled to heat the first water-material mixture in the cooking chamber of the food processor with a second heating power. The third water-ingredient mixture is heated to maintain its temperature at a first temperature, and the stirring device is controlled to stir the third water-ingredient mixture at a third stirring speed to obtain a fourth water-ingredient mixture. When the first temperature is maintained for a first preset duration, the food processor enters a slow boiling and thickening stage. According to the third heating parameters, the heating device is controlled to heat the fourth water-ingredient mixture in the food processor's cooking chamber to obtain a fifth water-ingredient mixture. When the third temperature is maintained for a second preset duration, the food processor enters an emulsification and pulping stage. According to the fourth stirring parameters, the stirring device is controlled to pulverize the fifth water-ingredient mixture to form a slurry. Through these specific parameter settings, unlike the cooking methods of fully raw or fully cooked grinding, this slurry production ensures double the extraction of soluble solids (nutrients) while reducing undesirable flavor compounds. Furthermore, it addresses the issue of overflow during mechanical heating in raw grinding from a process integration perspective, resulting in a slurry with a significantly thicker texture.

[0153] Please see Figure 7 , Figure 7 This is a schematic flowchart of a pulping control method provided in an embodiment of this application. Figure 7 As shown, the method in this application embodiment may include the following steps S401-S404.

[0154] S401, Oxygen removal stage: The water-material mixture is heated to temperature T1 with heating power P1, wherein T1 is greater than or equal to 78℃ and less than or equal to 82℃, P1 is greater than or equal to 1000w and less than or equal to 1200w, and the water-material mixture is stirred without pulverization at a first stirring speed r1 and a first stirring time at a first preset interval, wherein r1 is greater than or equal to 1000r / min and less than or equal to 3000r / min;

[0155] In one embodiment, the pulping control method includes four control stages: an oxygen removal stage, a coarse grinding stage, a slow boiling and thickening stage, and an emulsification pulping stage. In the oxygen removal stage, the water-material mixture is rapidly heated to temperature T1 at a power of 1000–1200 W, quickly bypassing the temperature range with higher levels of fishy-smelling substances, further reducing the production of these substances. Specifically, at temperatures between 78℃ and T1, and between 82℃, cooking at this temperature does not produce fishy-smelling substances. Simultaneously, non-grinding stirring is performed at a speed of 1000 r / min ≤ r1 ≤ 3000 r / min to promote the removal of oxygen from the water during heating and increase the concentration of hydrogen ions ionized in the water, thus lowering the pH and creating a weakly acidic, low-oxygen environment, allowing the seed coat of the pulping material to fully absorb water and expand. It should be noted that non-grinding stirring means that the food particles are not cut during the stirring process; the vast majority of the food particles remain in their initial, intact state, or if any are cut, only a very small number are cut, and the cut particles have no impact on the overall cooking effect. The first preset interval can be 1 minute, and the first stirring time is greater than 0 and less than or equal to 6 seconds. Preferably, the first stirring time is 5 seconds.

[0156] S402, coarse crushing stage: After the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min;

[0157] Specifically, the deoxygenation stage ends after the temperature of the water-material mixture reaches T1. The coarse grinding stage performs preliminary grinding on the water-material mixture in a weakly acidic and low-oxygen environment, cutting the initial particles in the water-material mixture into smaller lumps. If the pulping material is ground too finely, it will promote the release of lipoxygenase, which will produce a fishy smell. Therefore, by controlling the rotation speed r2 to be greater than or equal to 4000 r / min and less than or equal to 6000 r / min and the stirring time t2 to be greater than or equal to 0.5 min and less than or equal to 1.5 min, the particle size after stirring can be controlled to prevent it from becoming too small, thereby breaking down the cage of nutrients and promoting the precipitation of solids. Furthermore, at the T1 temperature, lipoxygenase is less active, which can effectively reduce the beany smell caused by lipoxygenation.

[0158] Optionally, the pulping control method may also include a solids precipitation stage. After the coarse grinding stage, the constant temperature is maintained for time t2 (T1). During the process, the mixture is stirred at an ultra-low speed (less than or equal to 3000 r / min, greater than or equal to 1000 r / min) for 5 seconds every 30 seconds to promote the precipitation of solids in the beans in a weakly acidic and low-oxygen environment, reduce oxidation, and reduce the oxidative loss of protein and fat while ensuring that the fishy smell substances are reduced and the soluble solids of the finished product are increased.

[0159] S403, slow boiling enrichment stage: heating to the third temperature T2 = T boiling point - 5℃ at an average heating rate K, where K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min;

[0160] Specifically, during the slow boiling and concentration stage, the average heating rate is controlled at 1.2℃ / min≤K≤2.0℃ / min. The coarsely crushed water-material mixture is slowly heated to T2=T boiling point-5℃ to complete the inactivation of anti-nutritional factors and softening of the material. Since the material softens during the heating and cooking process, it is easier to crush and pulp in the subsequent process, which helps to improve the crushing efficiency.

[0161] S404, Emulsification and Pulping Stage: After the slow boiling and thickening stage is completed, the mixture is intermittently stirred at a stirring speed r3, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is followed by a second preset interval, and the cumulative stirring time is t3, which is greater than or equal to 15 min and less than or equal to 25 min.

[0162] Specifically, the emulsification and pulping are completed by pulverizing in a high-temperature environment. The stirring speed r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. At this speed, the small pieces of material can be fully ground and pulverized, making the pulp more delicate. Intermittent stirring can be used, with a second preset interval between the third stirring time and the third stirring time, and a cumulative stirring time of 15 min to 25 min, to obtain a pulp with a delicate taste.

[0163] Optionally, during the emulsification pulping stage, auxiliary heating is provided between multiple pulping intervals to maintain the pulp temperature at or near T2.

[0164] In this embodiment, the deoxygenation stage creates a low-oxygen, weakly acidic environment for the water-material mixture, which helps reduce undesirable flavor substances produced by oxidation reactions and allows the seed coat to fully absorb water and expand. Then, in the coarse crushing stage, since the seed coat has already fully absorbed water and expanded, medium-speed crushing at 4000-6000 r / min breaks the material into small particles, thus destroying the nutrient cage and making it easier to release nutrients. Simultaneously, this stage maintains a low-oxygen, weakly acidic environment, preventing the release of excessive fishy odors due to material breakage. Flavoring substances are first extracted, and then the mixture enters a slow boiling and concentration stage. By heating the water-material mixture to T2 (T2 = T boiling point - 5℃), anti-nutritional factors such as trypsin inhibitors and lipoxygenases in the water-material mixture are inactivated, and the beans are softened. Finally, the mixture is pulverized at high temperature to complete emulsification and pulping. During the process, the motor stirs the mixture at a speed of r3 (15000r / min ≥ r3 ≥ 10000r / min) to complete the pulverization, promote the integration of nutrients, and ensure that the oil is fully emulsified, resulting in a smooth-tasting and nutrient-rich pulp.

[0165] Please see Figure 8 , Figure 8 This is a schematic flowchart of a pulping control method provided in an embodiment of this application. Figure 8 As shown, the method in this application embodiment may include the following steps S501-S104.

[0166] S501, coarse crushing stage: After the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min;

[0167] In one embodiment, the pulping control method includes four control stages: a coarse grinding stage, a solids precipitation stage, a slow boiling and thickening stage, and an emulsification pulping stage. In the coarse grinding stage, the water-material mixture is initially ground at temperature T1, cutting the initial particles in the mixture into smaller lumps. If the pulping material is ground too finely, it will promote the release of lipoxygenase, leading to a fishy odor. Therefore, by controlling the rotation speed r2 to be greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and the stirring time t2 to be greater than or equal to 0.5 min and less than or equal to 1.5 min, the particle size after stirring can be controlled to prevent it from becoming too small, thereby breaking down the nutrient cage and promoting solids precipitation. In a feasible embodiment, T1 is greater than or equal to 78°C and less than or equal to 82°C. At temperature T1, lipoxygenase is less active, effectively reducing the beany odor caused by lipoxygenation.

[0168] Optionally, an oxygen removal stage may be included before the coarse grinding stage. This stage involves heating and intermittent stirring to reach temperature T1. Specifically, the heating power P1 is greater than or equal to 1000W and less than or equal to 1200W. The water-material mixture is stirred without grinding at a first stirring speed r1 and a first stirring time at preset intervals, where 1000r / min ≤ r1 ≤ 3000r / min. This low-speed stirring promotes the removal of oxygen from the water during the heating process and increases the concentration of hydrogen ions ionized in the water, thus lowering the pH and creating a weakly acidic, low-oxygen environment. Under this environment, the material is less prone to oxidation, reducing the generation of undesirable flavor compounds.

[0169] S502, Solid precipitation stage: After the coarse crushing stage is completed, maintain the constant temperature T1 for a preset time of 10min≤t1≤20min. During the constant temperature period, stir the water-material mixture at a stirring speed of 1000r / min≤r1≤3000r / min every first preset interval.

[0170] Specifically, after the coarse crushing stage, the temperature is maintained at T1 for 10-20 minutes. During the constant temperature period, the water-material mixture is stirred at a low speed of 1000 r / min ≤ r1 ≤ 3000 r / min at each first preset interval. Stirring at this speed can promote the precipitation of solids in a weakly acidic and low-oxygen environment, reduce oxidation, reduce the oxidative loss of protein and fat, and ensure that the fishy smell substances are reduced and the soluble solids of the finished product are increased.

[0171] In related technologies, pulping is done using a pure raw grinding method, where the pulp is crushed in cold water and then directly heated for grinding. In this cooking method, the solids are in an active state, making them more prone to boiling over during heating. In contrast, this solution uses two stages: coarse crushing and solids precipitation. Grinding and heating are performed separately to promote solids precipitation, while minimizing the risk of boiling over.

[0172] S503, slow boiling enrichment stage: heating to the third temperature T2 = T boiling point - 5℃ at an average heating rate K, where K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min;

[0173] Specifically, during the slow boiling and concentration stage, the average heating rate is controlled at 1.2℃ / min≤K≤2.0℃ / min. The coarsely crushed water-material mixture is slowly heated to T2=T boiling point-5℃ to complete the inactivation of anti-nutritional factors and softening of the material. Since the material softens during the heating and cooking process, it is easier to crush and pulp in the subsequent process, which helps to improve the crushing efficiency.

[0174] S504, Emulsification and Pulping Stage: After the slow boiling and thickening stage is completed, the mixture is intermittently stirred at a stirring speed r3, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is followed by a second preset interval, and the cumulative stirring time is t3, which is greater than or equal to 15 min and less than or equal to 25 min.

[0175] Specifically, the emulsification and pulping are completed by pulverizing in a high-temperature environment. The stirring speed r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. At this speed, the small pieces of material can be fully ground and pulverized, making the pulp more delicate. Intermittent stirring can be used, with a second preset interval between the third stirring time and the third stirring time, and a cumulative stirring time of 15 min to 25 min, to obtain a pulp with a delicate taste.

[0176] In this embodiment, the material is initially crushed into small particles at T1 through a coarse crushing stage, which breaks down the nutrient cage of the material and promotes the precipitation of solids. Then, it is slowly stirred at a constant temperature of 1000r / min≤r1≤3000r / min at T1 to promote the release of nutrients (solids) at this temperature. At the same time, the oxidation loss of proteins and fats is reduced at this temperature, which ensures that the fishy smell is reduced. Then, the harmful substances (such as anti-protein factors) are inactivated through a slow boiling concentration stage, and the material particles are fully softened by absorbing water. The high-speed grinding in the emulsification pulping stage further promotes the precipitation of nutrients and ensures that the oil is fully emulsified, thereby improving the nutritional value and taste of the obtained pulp.

[0177] Please see Figure 9 , Figure 9 This is a schematic flowchart of a pulping control method provided in an embodiment of this application. Figure 9 As shown, the method in this application embodiment may include the following steps S601-S604.

[0178] S601, Oxygen removal stage: The water-material mixture is heated to temperature T1 with heating power P1, wherein T1 is greater than or equal to 78℃ and less than or equal to 82℃, P1 is greater than or equal to 1000w and less than or equal to 1200w, and the water-material mixture is stirred without pulverization at a first stirring speed r1 and a first stirring time at a first preset interval, wherein r1 is greater than or equal to 1000r / min and less than or equal to 3000r / min;

[0179] In one embodiment, the pulping control method includes four control stages: an oxygen removal stage, a solids precipitation stage, a slow boiling and thickening stage, and an emulsification pulping stage. In the oxygen removal stage, the water-material mixture is rapidly heated to temperature T1 at a power of 1000–1200 W, quickly bypassing the temperature range with higher levels of fishy-smelling substances, further reducing the production of these substances. Specifically, at temperatures between 78℃ and T1, and between 82℃, cooking at this temperature does not produce fishy-smelling substances. Simultaneously, non-crushing stirring is performed at a speed of 1000 r / min ≤ r1 ≤ 3000 r / min to promote the removal of oxygen from the water during heating and increase the concentration of hydrogen ions ionized in the water, thus lowering the pH and creating a weakly acidic, low-oxygen environment, allowing the seed coat of the pulping material to fully absorb water and expand. It should be noted that non-crushing stirring means that the food particles are not cut during the stirring process; the vast majority of the food particles remain in their initial, intact state, or if any are cut, only a very small number are cut, and the cut particles have no impact on the overall cooking effect. The first preset interval can be 1 minute, and the first stirring time is greater than 0 and less than or equal to 6 seconds. Preferably, the first stirring time is 5 seconds.

[0180] S602, coarse crushing stage: After the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min;

[0181] Specifically, the deoxygenation stage ends after the temperature of the water-material mixture reaches T1. The coarse grinding stage performs preliminary grinding on the water-material mixture in a weakly acidic and low-oxygen environment, cutting the initial particles in the water-material mixture into smaller lumps. If the pulping material is ground too finely, it will promote the release of lipoxygenase, which will produce a fishy smell. Therefore, by controlling the rotation speed r2 to be greater than or equal to 4000 r / min and less than or equal to 6000 r / min and the stirring time t2 to be greater than or equal to 0.5 min and less than or equal to 1.5 min, the particle size after stirring can be controlled to prevent it from becoming too small, thereby breaking down the cage of nutrients and promoting the precipitation of solids. Furthermore, at the T1 temperature, lipoxygenase is less active, which can effectively reduce the beany smell caused by lipoxygenation.

[0182] S603, Solid precipitation stage: After the coarse crushing stage is completed, maintain the constant temperature T1 for a preset time of 10min≤t4≤20min. During the constant temperature period, stir the water-material mixture at a stirring speed of 1000r / min≤r4≤3000r / min every third preset interval.

[0183] Specifically, after the coarse crushing stage, the temperature is maintained at T1 for 10–20 minutes. During this constant temperature period, the water-material mixture is stirred at a low speed of 1000 r / min ≤ r1 ≤ 3000 r / min at third preset intervals. Stirring at this speed promotes the precipitation of solids in a weakly acidic, low-oxygen environment, reducing oxidation. This minimizes the oxidative loss of proteins and fats while reducing odorous substances and increasing the soluble solids content of the finished product. The third preset interval is 30 seconds, and each stirring session can last for 5 seconds.

[0184] S604, Emulsification and Pulping Stage: Heat to T2, where T2 is greater than T1, and intermittently stir at a stirring speed r, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is followed by a second preset interval, and the cumulative stirring time is t3, which satisfies the condition of being greater than or equal to 15 min and less than or equal to 25 min.

[0185] Specifically, the water-material mixture is heated to T2 to inactivate the anti-nutritional factors, and then pulverized at high temperature (T2) through high-speed intermittent stirring to complete the emulsification and slurry preparation. The stirring speed r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. At this speed, small pieces of material can be thoroughly ground and pulverized, resulting in a more delicate slurry texture. Intermittent stirring can be used, with a second preset interval between the third stirring time and the third stirring time, for a total stirring time of 15 min to 25 min, to obtain a slurry with a delicate texture.

[0186] In this embodiment, the deoxygenation stage creates a low-oxygen, weakly acidic environment for the water-material mixture, which helps reduce undesirable flavor substances produced by oxidation reactions and allows the seed coat to fully absorb water and expand. Then, the mixture enters the coarse grinding stage, where the material is initially crushed into small particles at T1, breaking down the nutrient cage and promoting the precipitation of solids. Afterward, slow stirring is performed at a constant temperature of T1 at 1000 r / min ≤ r1 ≤ 3000 r / min to promote the release of nutrients (solids) at this temperature. Simultaneously, this temperature reduces the oxidative loss of proteins and fats, ensuring a reduction in fishy-smelling substances. Finally, the water-material mixture is heated to a high temperature of T2 and ground at high speed in the emulsification and pulping stage, further promoting the precipitation of nutrients and ensuring complete emulsification of oils, thus improving the nutritional value and taste of the resulting slurry.

[0187] Please see Figure 10 , Figure 10 This is a schematic flowchart of a pulping control method provided in an embodiment of this application. Figure 10As shown, the method in this application embodiment may include the following steps S701-S704.

[0188] S701, coarse crushing stage: After the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min;

[0189] In one embodiment, the pulping control method includes four control stages: a coarse grinding stage, a solid precipitation stage, a slow boiling concentration stage, and an emulsification pulping stage. In the emulsification pulping stage, the pulp can also be reheated.

[0190] Specifically, in the coarse crushing stage, the water-material mixture is initially crushed at temperature T1, cutting the initial particles in the mixture into smaller lumps. If the pulping material is crushed too finely, it will promote the release of lipoxygenase, which will produce a fishy smell. Therefore, by controlling the rotation speed r2 to be greater than or equal to 4000 r / min and less than or equal to 6000 r / min and the stirring time t2 to be greater than or equal to 0.5 min and less than or equal to 1.5 min, the particle size after stirring can be controlled to be not too small, thereby breaking down the cage of nutrients and promoting the precipitation of solids. In one feasible implementation, T1 is greater than or equal to 78°C and less than or equal to 82°C. At temperature T1, lipoxygenase is not easily activated, which can effectively reduce the beany smell caused by lipoxygenation.

[0191] Optionally, an oxygen removal stage may be included before the coarse grinding stage. This stage involves heating and intermittent stirring to reach temperature T1. Specifically, the heating power P1 is greater than or equal to 1000W and less than or equal to 1200W. The water-material mixture is stirred without grinding at a first stirring speed r1 and a first stirring time at preset intervals, where 1000r / min ≤ r1 ≤ 3000r / min. This low-speed stirring promotes the removal of oxygen from the water during the heating process and increases the concentration of hydrogen ions ionized in the water, thus lowering the pH and creating a weakly acidic, low-oxygen environment. Under this environment, the material is less prone to oxidation, reducing the generation of undesirable flavor compounds.

[0192] S702, Solid precipitation stage: After the coarse crushing stage is completed, maintain the constant temperature T1 for a preset time of 10min≤t1≤20min. During the constant temperature period, stir the water-material mixture at a stirring speed of 1000r / min≤r1≤3000r / min every first preset interval.

[0193] Specifically, after the coarse crushing stage, the temperature is maintained at T1 for 10-20 minutes. During the constant temperature period, the water-material mixture is stirred at a low speed of 1000 r / min ≤ r1 ≤ 3000 r / min at each first preset interval. Stirring at this speed can promote the precipitation of solids in a weakly acidic and low-oxygen environment, reduce oxidation, reduce the oxidative loss of protein and fat, and ensure that the fishy smell substances are reduced and the soluble solids of the finished product are increased.

[0194] S703, slow boiling enrichment stage: heating to the third temperature T2 = T boiling point - 5℃ at an average heating rate K, where K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min;

[0195] Specifically, during the slow boiling and concentration stage, the average heating rate is controlled at 1.2℃ / min≤K≤2.0℃ / min. The coarsely crushed water-material mixture is slowly heated to T2=T boiling point-5℃ to complete the inactivation of anti-nutritional factors and softening of the material. Since the material softens during the heating and cooking process, it is easier to crush and pulp in the subsequent process, which helps to improve the crushing efficiency.

[0196] S704, Emulsification and Pulping Stage: After the slow boiling and thickening stage is completed, the mixture is intermittently stirred at a stirring speed r3, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is followed by a second preset interval, and the cumulative stirring time is t3. t3 is greater than or equal to 15 min and less than or equal to 25 min. The temperature of the water-material mixture is detected within each second preset interval. When the temperature is lower than T3, heating power P2 is used to supplement the heat.

[0197] Specifically, after heating is complete, emulsification and slurry preparation are performed under high-temperature conditions. The stirring speed r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. At this speed, small pieces of material are thoroughly ground, resulting in a smoother slurry texture. Intermittent stirring can be used, with a second preset interval between the third stirring session, for a total stirring time of 15-25 minutes, yielding a slurry with a smooth texture. During the stirring intervals, the temperature of the water-material mixture can be monitored. If the temperature drops below the preset temperature T3, heating power P2 is used to raise the temperature of the water-material mixture to T3, preventing temperature drops due to intermittent stirring and affecting the emulsification effect. After the interval ends, grinding resumes. P2 = 300-400 W; using lower power for supplemental heating and temperature maintenance prevents scorching and boiling over. For example, T3 = Tboiling point - 10°C. At this temperature, stirring allows for better emulsification of fats and better integration with other nutrients.

[0198] In this embodiment, the material is initially crushed into small particles at T1 through a coarse crushing stage, breaking down the nutrient cage of the material and promoting the precipitation of solids. Then, it is slowly stirred at a constant temperature of 1000r / min≤r1≤3000r / min at T1 to promote the release of nutrients (solids) at this temperature, reduce the oxidative loss of protein and fat, and effectively deactivate endogenous oxidase activity at this temperature, thereby inhibiting the production of beany odor. After that, the harmful substances (such as anti-protein factors) are inactivated through a slow boiling and concentration stage, and the material particles are fully softened by absorbing water. The high-speed grinding in the emulsification and pulping stage further promotes the precipitation of nutrients. The temperature is monitored during the stirring interval to ensure that the oil and fat are fully emulsified at the specified temperature, thereby improving the nutritional content and taste of the obtained pulp.

[0199] based on Figure 1-2 The following will combine a food processor with... Figures 11-15 This application provides a detailed description of the control device provided in its embodiments. It should be noted that... Figures 11-15 The pulping control device in the present application is used to perform the pulping control device. Figures 3-10 The methods shown in the embodiments are for illustrative purposes only, illustrating the parts relevant to the embodiments of this application. For specific technical details not disclosed, please refer to this application. Figures 3-10 The example shown.

[0200] Please see Figure 11 , Figure 11 This is a schematic diagram of a pulping control device provided in an embodiment of this application. Figure 11 As shown, the pulping control device 11 in this application embodiment may include: a first control unit 81, a second control unit 82, a third control unit 83, a fourth control unit 84, and a fifth control unit 85.

[0201] The first control unit 81 is used to respond to the cooking execution command, and when the food processor enters the oxygen removal stage, it controls the heating device to heat the first water-material mixture in the cooking chamber of the food processor according to the first heating parameters, and controls the stirring device to stir the first water-material mixture according to the first stirring parameters to obtain the second water-material mixture.

[0202] The second control unit 82 is used to control the mixing device to crush the second water-material mixture according to the second mixing parameters when the food processor enters the coarse crushing stage, so as to obtain a third water-material mixture; the average particle size of the material particles in the third water-material mixture is smaller than the average particle size of the material particles in the second water-material mixture.

[0203] The third control unit 83 is used to control the heating device to maintain the temperature of the third water mixture at the first temperature according to the second heating parameters when the food processor enters the solids precipitation stage, and to control the stirring device to stir the third water mixture according to the third stirring parameters to obtain the fourth water mixture.

[0204] The fourth control unit 84 is used to control the heating device to heat the fourth water mixture according to the third heating parameters when the food processor enters the slow boiling and thickening stage, so as to obtain the fifth water mixture.

[0205] The fifth control unit 85 is used to control the stirring device to crush the fifth water-material mixture according to the fourth stirring parameters when the food processor enters the emulsification and pulping stage, so as to form a slurry from the fifth water-material mixture.

[0206] Optionally, the food processor also includes a water injection device, and the first control unit 81 is specifically used to determine the set amount of pulp corresponding to the cooking execution command in response to the cooking execution command;

[0207] The water injection device injects water into the cooking chamber of the food processor according to the set pulping volume;

[0208] Once the water level in the cooking chamber meets the set pulping volume, the food processor enters the oxygen removal stage. The heating device is controlled according to the first heating parameter to heat the first water-material mixture in the cooking chamber of the food processor, and the stirring device is controlled according to the first stirring parameter to stir the first water-material mixture to obtain the second water-material mixture.

[0209] Optionally, the first control unit 81 is specifically used to control the heating device to heat the first water-ingredient mixture in the cooking cavity of the food processor with a first heating power until the temperature of the first water-ingredient mixture reaches a second temperature.

[0210] Optionally, the first heating power P1 satisfies that P1 is greater than or equal to 1000W and less than or equal to 1200W, and the second temperature T1 satisfies that it is greater than or equal to 78℃ and less than or equal to 82℃.

[0211] Optionally, the first control unit 81 is specifically used to control the stirring device to stir the first water-material mixture at a first stirring speed.

[0212] Optionally, the first control unit 81 is specifically used to control the stirring device to stir the first water-material mixture at a first stirring speed at each first preset interval, and the stirring time is the first stirring time.

[0213] Optionally, the first stirring speed is the minimum speed allowed by the stirring device motor.

[0214] Optionally, the minimum permissible speed of the motor is greater than 1000 r / min and less than 3000 r / min.

[0215] Optionally, the first preset interval duration t1 satisfies that t1 is greater than or equal to 50s and less than or equal to 70s, and the first stirring duration t2 satisfies that t2 is greater than 0s and less than or equal to 6s.

[0216] Optionally, the second control unit 82 is specifically used to control the stirring device to crush the second water-material mixture at a second stirring speed when the food processor enters the coarse crushing stage, and the stirring time is a second stirring time, so as to obtain a third water-material mixture.

[0217] Optionally, the second stirring speed r2 satisfies that r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and the second stirring time t3 is greater than or equal to 0.5 min and less than or equal to 1.5 min.

[0218] Optionally, the third control unit 83 is specifically used to control the heating device to heat the third water-material mixture in the cooking chamber of the food processor with a second heating power when the food processor enters the solids precipitation stage, so as to maintain the temperature of the third water-material mixture at a first temperature.

[0219] Optionally, the third control unit 83 is specifically used to control the stirring device to stir the third water-material mixture at a third stirring speed.

[0220] Optionally, the third control unit 83 is specifically used to control the stirring device to stir the third water-material mixture at a third stirring speed at every second preset interval, and the stirring time is the third stirring time.

[0221] Optionally, the second preset interval t4 satisfies that t4 is greater than or equal to 25s and less than or equal to 35s, the third stirring speed r3 satisfies that r3 is greater than 1000r / min and less than 3000r / min, and the third stirring duration t5 satisfies that t5 is greater than 0s and less than or equal to 6s.

[0222] Optionally, the fourth control unit 84 is specifically used to determine that the food processor has entered the slow boiling and thickening stage after the first temperature is maintained for a first preset time, and to control the heating device to heat the fourth water-material mixture in the cooking chamber of the food processor according to the third heating parameters, so as to obtain the fifth water-material mixture.

[0223] Optionally, the fourth control unit 84 is specifically used to control the heating device to heat the fourth water-ingredient mixture at a preset heating rate when the food processor enters the slow boiling and thickening stage, until the temperature of the fourth water-ingredient mixture reaches the third temperature, so as to obtain the fifth water-ingredient mixture.

[0224] Optionally, the preset heating rate K satisfies that K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min.

[0225] Optionally, the fifth control unit 85 is specifically used to determine that the food processor has entered the emulsification and pulping stage after the third temperature has been maintained for a second preset time, and to control the stirring device to crush the fifth water-material mixture according to the fourth stirring parameters so that the fifth water-material mixture forms a slurry.

[0226] Optionally, the fifth control unit 85 is specifically used to control the stirring device to crush the fifth water-material mixture at a fourth stirring speed every third preset interval, the stirring time being the fourth stirring time, until the cumulative stirring time reaches the fifth stirring time.

[0227] Optionally, the fourth stirring speed r4 satisfies that r4 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min, and the fifth stirring time t6 satisfies that t6 is greater than or equal to 15 min and less than or equal to 25 min.

[0228] Optionally, the fifth control unit 85 is also used to detect the temperature of the fifth water-material mixture during each third interval, and when the temperature is lower than the fourth temperature, control the heating device to heat the fifth water-material mixture according to the fourth heating parameters so that the temperature of the fifth water-material mixture reaches the fourth temperature.

[0229] Optionally, the fifth control unit 85 is also configured to control the heating device to heat the fourth water-material mixture at a third heating power when the temperature is lower than the fourth temperature, until the temperature of the fourth water-material mixture reaches the fourth temperature.

[0230] Please see Figure 12 , Figure 12 This is a schematic diagram of a pulping control device provided in an embodiment of this application. Figure 12 As shown, the pulping control device 12 in this embodiment may include: a first control unit 91, a second control unit 92, a fourth control unit 94 and a fifth control unit 95.

[0231] The first control unit 91 is used for the oxygen removal stage: heating the water-material mixture to a temperature T1 with a heating power P1, wherein T1 is greater than or equal to 78°C and less than or equal to 82°C, P1 is greater than or equal to 1000W and less than or equal to 1200W, and stirring the water-material mixture without pulverizing at a first stirring speed r1 and a first stirring time at a first preset interval, wherein r1 is greater than or equal to 1000r / min and less than or equal to 3000r / min;

[0232] The second control unit 92 is used for the coarse crushing stage: after the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min;

[0233] The fourth control unit 94 is used for the slow boiling enrichment stage: heating to the third temperature T2 = T boiling point - 5℃ at an average heating rate K, wherein K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min;

[0234] The fifth control unit 95 is used for the emulsification and pulping stage: after the slow boiling and thickening stage is completed, the stirring is intermittently at a stirring speed r3, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is separated by a second preset interval, and the cumulative stirring time t3 is 15 min greater than or equal to 15 min and less than or equal to 25 min.

[0235] Please see Figure 13 , Figure 13 This is a schematic diagram of a pulping control device provided in an embodiment of this application. Figure 13 As shown, the pulping control device 13 in this application embodiment may include: a second control unit 1002, a third control unit 1003, a fourth control unit 1004 and a fifth control unit 1005.

[0236] The second control unit 1002 is used in the coarse crushing stage: after the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min;

[0237] The third control unit 1003 is used for the solid precipitation stage: after the coarse crushing stage is completed, the constant temperature T1 is maintained for a preset time of 10min≤t1≤20min. During the constant temperature period, the water-material mixture is stirred at a stirring speed of 1000r / min≤r1≤3000r / min every first preset interval.

[0238] The fourth control unit 1004 is used for the slow boiling enrichment stage: heating to the third temperature T2 = T boiling point - 5℃ at an average heating rate K, wherein K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min;

[0239] The fifth control unit 1005 is used in the emulsification and pulping stage: after the slow boiling and thickening stage is completed, it is intermittently stirred at a stirring speed r3, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is separated by a second preset interval, and the cumulative stirring time t3 is 15 min greater than or equal to 15 min and less than or equal to 25 min.

[0240] Please see Figure 14 , Figure 14 This is a schematic diagram of a pulping control device provided in an embodiment of this application. Figure 14 As shown, the pulping control device 14 in this application embodiment may include: a first control unit 1101, a second control unit 1102, a third control unit 1103 and a fifth control unit 1105.

[0241] The first control unit 1101 is used in the oxygen removal stage: heating the water-material mixture to a temperature T1 with a heating power P1, wherein T1 is greater than or equal to 78°C and less than or equal to 82°C, P1 is greater than or equal to 1000W and less than or equal to 1200W, and stirring the water-material mixture without pulverizing at a first stirring speed r1 and a first stirring time at a first preset interval, wherein r1 is greater than or equal to 1000r / min and less than or equal to 3000r / min;

[0242] The second control unit 1102 is used for the coarse crushing stage: after the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min;

[0243] The third control unit 1103 is used for the solid precipitation stage: after the coarse crushing stage is completed, the constant temperature T1 is maintained for a preset time of 10min≤t4≤20min. During the constant temperature period, the water-material mixture is stirred at a stirring speed of 1000r / min≤r4≤3000r / min every third preset interval.

[0244] The fifth control unit 1105 is used in the emulsification and pulping stage: heating to T2, where T2 is greater than T1, intermittently stirring at a stirring speed r, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min, with a second preset interval between each third stirring time, and a cumulative stirring time t3, where t3 satisfies greater than or equal to 15 min and less than or equal to 25 min.

[0245] Please see Figure 15 , Figure 15 This is a schematic diagram of a pulping control device provided in an embodiment of this application. Figure 15 As shown, the pulping control device 15 in this application embodiment may include: a second control unit 1202, a third control unit 1203, a fourth control unit 1204 and a fifth control unit 1205.

[0246] The second control unit 1202 is used for the coarse crushing stage: after the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min;

[0247] The third control unit 1203 is used for the solid precipitation stage: after the coarse crushing stage is completed, the constant temperature T1 is maintained for a preset time of 10min≤t1≤20min. During the constant temperature period, the water-material mixture is stirred at a stirring speed of 1000r / min≤r1≤3000r / min every first preset interval.

[0248] The fourth control unit 1204 is used for the slow boiling enrichment stage: heating to the third temperature T2 = T boiling point - 5℃ at an average heating rate K, wherein K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min;

[0249] The fifth control unit 1205 is used in the emulsification and pulping stage: after the slow boiling and thickening stage is completed, it is intermittently stirred at a stirring speed r3, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is followed by a second preset interval, and the cumulative stirring time t3 is 15 min or less than or equal to 25 min. The temperature of the water-material mixture is detected within each second preset interval. When the temperature is lower than T3, the heating power P2 is used to supplement the heat.

[0250] Please see Figure 16 , Figure 16 This is a schematic diagram of the structure of a food processor provided in an embodiment of this application.

[0251] For example, such as Figure 16 As shown, the food processor 100 includes a processor 101 and a memory 102, wherein the processor 101 is electrically connected to the memory 102.

[0252] The processor 101 is the control center of the food processor 100 and may include one or more processing cores. The processor 101 connects to various parts of the food processor using various interfaces and lines. By running or calling computer programs stored in the memory 102, and by calling data stored in the memory 102, it executes various functions and processes data of the food processor, thereby providing overall control of the food processor 100. Optionally, the processor 101 may be implemented using at least one of the following hardware forms: Digital Signal Processing (DSP), Field Programmable Gate Array (FPGA), and Programmable Logic Array (PLA). The processor 101 may integrate one or more of the following: CPU, Graphics Processing Unit (GPU), and modem. The CPU primarily handles the operating system, user page, and applications; the GPU is responsible for rendering and drawing the displayed content; and the modem handles wireless communication. It is understood that the modem may also not be integrated into the processor 101 and may be implemented separately using a communication chip.

[0253] The memory 102 can be used to store software programs and modules. The processor 101 executes various functional applications and data processing by running the computer programs and modules stored in the memory 102. The memory 102 may mainly include a program storage area and a data storage area. The program storage area may store the operating system, computer programs required for at least one function, etc.; the data storage area may store data created based on the use of the food processor 100, etc.

[0254] Furthermore, memory 102 may include high-speed random access memory, and may also include non-volatile memory, such as at least one disk storage device, flash memory device, or other volatile solid-state storage device. Accordingly, memory 102 may also include a memory controller to provide processor 101 with access to memory 102.

[0255] In this embodiment, the processor 101 in the food processor 100 loads the instructions corresponding to the processes of one or more computer programs into the memory 102 according to the following steps, and the processor 101 runs the computer programs stored in the memory 102 to realize various functions, as follows:

[0256] In response to the cooking execution command, when the food processor enters the oxygen removal stage, the heating device is controlled to heat the first water-material mixture in the cooking chamber of the food processor according to the first heating parameter, and the stirring device is controlled to stir the first water-material mixture according to the first stirring parameter to obtain the second water-material mixture.

[0257] When the food processor enters the coarse grinding stage, the mixing device is controlled according to the second mixing parameters to grind the second water-material mixture to obtain the third water-material mixture; the average particle size of the material particles in the third water-material mixture is smaller than the average particle size of the material particles in the second water-material mixture.

[0258] When the food processor enters the solids separation stage, the heating device is controlled according to the second heating parameter to maintain the temperature of the third water mixture at the first temperature, and the stirring device is controlled according to the third stirring parameter to stir the third water mixture to obtain the fourth water mixture.

[0259] When the food processor enters the slow boiling and thickening stage, the heating device is controlled according to the third heating parameter to heat the fourth water mixture to obtain the fifth water mixture.

[0260] When the food processor enters the emulsification and pulping stage, the mixing device is controlled according to the fourth mixing parameter to crush the fifth water-material mixture so that the fifth water-material mixture forms a slurry.

[0261] Optionally, the food processor also includes a water injection device. When the processor 101 executes a cooking execution command, and the food processor enters the oxygen degassing stage, it controls the heating device to heat the first water-material mixture in the cooking chamber of the food processor according to the first heating parameters, and controls the stirring device to stir the first water-material mixture according to the first stirring parameters to obtain a second water-material mixture, specifically performing the following:

[0262] In response to the cooking execution command, determine the set pulping amount corresponding to the cooking execution command;

[0263] The water injection device injects water into the cooking chamber of the food processor according to the set pulping volume;

[0264] Once the water level in the cooking chamber meets the set pulping volume, the food processor enters the oxygen removal stage. The heating device is controlled according to the first heating parameter to heat the first water-material mixture in the cooking chamber of the food processor, and the stirring device is controlled according to the first stirring parameter to stir the first water-material mixture to obtain the second water-material mixture.

[0265] Optionally, when the processor 101 controls the heating device to heat the first water-material mixture in the cooking cavity of the food processor according to the first heating parameters, it specifically performs the following:

[0266] The heating device is controlled to heat the first water-ingredient mixture in the cooking chamber of the food processor with a first heating power until the temperature of the first water-ingredient mixture reaches a second temperature.

[0267] Optionally, the first heating power P1 satisfies that P1 is greater than or equal to 1000W and less than or equal to 1200W, and the second temperature T1 satisfies that it is greater than or equal to 78℃ and less than or equal to 82℃.

[0268] Optionally, when the processor 101 controls the stirring device to stir the first water-material mixture according to the first stirring parameters, it specifically performs the following:

[0269] The stirring device is controlled to stir the first water-material mixture at a first stirring speed.

[0270] Optionally, when the processor 101 controls the stirring device to stir the first water-material mixture at a first stirring speed, it specifically performs the following:

[0271] At each first preset interval, the stirring device is controlled to stir the first water-material mixture at a first stirring speed for a first stirring duration.

[0272] Optionally, the first stirring speed is the minimum speed allowed by the stirring device motor.

[0273] Optionally, the minimum permissible speed of the motor is greater than 1000 r / min and less than 3000 r / min.

[0274] Optionally, the first preset interval duration t1 satisfies that t1 is greater than or equal to 50s and less than or equal to 70s, and the first stirring duration t2 satisfies that t2 is greater than 0s and less than or equal to 6s.

[0275] Optionally, when the processor 101 controls the mixing device to pulverize the second water-material mixture according to the second mixing parameters to obtain the third water-material mixture during the coarse pulverization stage of the food processor, the specific execution is as follows:

[0276] When the food processor enters the coarse grinding stage, the stirring device is controlled to grind the second water-material mixture at the second stirring speed for the second stirring time to obtain the third water-material mixture.

[0277] Optionally, the second stirring speed r2 satisfies that r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and the second stirring time t3 is greater than or equal to 0.5 min and less than or equal to 1.5 min.

[0278] Optionally, when the processor 101 controls the heating device to maintain the temperature of the third water-material mixture at the first temperature according to the second heating parameters during the solids separation stage of the food processor, the specific execution is as follows:

[0279] When the food processor enters the solids separation stage, the heating device is controlled to heat the third water-material mixture in the cooking chamber of the food processor with a second heating power so that the temperature of the third water-material mixture is maintained at the first temperature.

[0280] Optionally, when the processor 101 controls the stirring device to stir the third water-material mixture according to the third stirring parameters, it specifically performs the following:

[0281] The stirring device is controlled to stir the third water-material mixture at a third stirring speed.

[0282] Optionally, when the processor 101 controls the stirring device to stir the third water-material mixture at a third stirring speed, it specifically performs the following:

[0283] At each second preset interval, the stirring device is controlled to stir the third water-material mixture at a third stirring speed for a third stirring duration.

[0284] Optionally, the second preset interval t4 satisfies that t4 is greater than or equal to 25s and less than or equal to 35s, the third stirring speed r3 satisfies that r3 is greater than 1000r / min and less than 3000r / min, and the third stirring duration t5 satisfies that t5 is greater than 0s and less than or equal to 6s.

[0285] Optionally, when the processor 101 controls the heating device to heat the fourth water-ingredient mixture in the cooking cavity of the food processor according to the third heating parameter during the slow boiling and thickening stage to obtain the fifth water-ingredient mixture, the processor 101 specifically performs the following:

[0286] Once the first temperature is maintained for a predetermined duration, the food processor enters the slow boiling and thickening stage. Based on the third heating parameters, the heating device is controlled to heat the fourth water-material mixture in the cooking chamber of the food processor to obtain the fifth water-material mixture.

[0287] Optionally, when the processor 101 controls the heating device to heat the fourth water-ingredient mixture according to the third heating parameter to obtain the fifth water-ingredient mixture during the slow boiling and thickening stage of the food processor, the specific execution is as follows:

[0288] When the food processor enters the slow boiling and thickening stage, the heating device is controlled to heat the fourth water mixture at a preset heating rate until the temperature of the fourth water mixture reaches the third temperature, so as to obtain the fifth water mixture.

[0289] Optionally, the preset heating rate K satisfies that K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min.

[0290] Optionally, when the processor 101 controls the mixing device to pulverize the fifth water-material mixture according to the fourth mixing parameters to form a slurry during the emulsification and pulping stage of the food processor, the specific execution is as follows:

[0291] Once the third temperature is maintained for the second preset duration, the food processor enters the emulsification and pulping stage. Based on the fourth stirring parameters, the stirring device is controlled to pulverize the fifth water-material mixture so that the fifth water-material mixture forms a slurry.

[0292] Optionally, when the processor 101 controls the stirring device to pulverize the fifth water-material mixture according to the fourth stirring parameters so that the fifth water-material mixture forms a slurry, it specifically performs the following:

[0293] Every third preset interval, the stirring device is controlled to crush the fifth water-material mixture at a fourth stirring speed for a fourth stirring time, until the cumulative stirring time reaches the fifth stirring time.

[0294] Optionally, the fourth stirring speed r4 satisfies that r4 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min, and the fifth stirring time t6 satisfies that t6 is greater than or equal to 15 min and less than or equal to 25 min.

[0295] Optionally, the processor 101 is also configured to: detect the temperature of the fifth water-material mixture during each third interval; and when the temperature is lower than the fourth temperature, control the heating device to heat the fifth water-material mixture according to the fourth heating parameters so that the temperature of the fifth water-material mixture reaches the fourth temperature.

[0296] Optionally, when the processor 101 executes the command to control the heating device to heat the fifth water-material mixture according to the fourth heating parameter when the temperature is lower than the fourth temperature, so that the temperature of the fifth water-material mixture reaches the fourth temperature, the processor 101 specifically executes the following:

[0297] When the temperature is lower than the fourth temperature, the heating device is controlled to heat the fourth water-material mixture at the third heating power until the temperature of the fourth water-material mixture reaches the fourth temperature.

[0298] Optionally, the processor 101 is also configured to perform: an oxygen removal stage: heating the water-material mixture to a temperature T1 with a heating power P1, wherein T1 is greater than or equal to 78°C and less than or equal to 82°C, P1 is greater than or equal to 1000W and less than or equal to 1200W, and stirring the water-material mixture without pulverizing at a first stirring speed r1 and a first stirring time at a first preset interval, wherein r1 is greater than or equal to 1000r / min and less than or equal to 3000r / min;

[0299] Coarse crushing stage: After the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min.

[0300] Slow boiling enrichment stage: Heat to the third temperature T2 = T boiling point - 5℃ at an average heating rate K, where K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min;

[0301] Emulsification and pulping stage: After the slow boiling and thickening stage is completed, the mixture is intermittently stirred at a stirring speed of r3, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is followed by a second preset interval, and the cumulative stirring time is t3, which is greater than or equal to 15 min and less than or equal to 25 min.

[0302] Optionally, the processor 101 is also used to perform: coarse crushing stage: after the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min;

[0303] Solid precipitation stage: After the coarse crushing stage is completed, maintain the constant temperature T1 for a preset time of 10min≤t1≤20min. During the constant temperature period, stir the water-material mixture at a stirring speed of 1000r / min≤r1≤3000r / min every first preset interval.

[0304] Slow boiling enrichment stage: Heat to the third temperature T2 = T boiling point - 5℃ at an average heating rate K, where K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min;

[0305] Emulsification and pulping stage: After the slow boiling and thickening stage is completed, the mixture is intermittently stirred at a stirring speed of r3, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is followed by a second preset interval, and the cumulative stirring time is t3, which is greater than or equal to 15 min and less than or equal to 25 min.

[0306] Optionally, the processor 101 is also configured to perform: an oxygen removal stage: heating the water-material mixture to a temperature T1 with a heating power P1, wherein T1 is greater than or equal to 78°C and less than or equal to 82°C, P1 is greater than or equal to 1000W and less than or equal to 1200W, and stirring the water-material mixture without pulverizing at a first stirring speed r1 and a first stirring time at a first preset interval, wherein r1 is greater than or equal to 1000r / min and less than or equal to 3000r / min;

[0307] Coarse crushing stage: After the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min.

[0308] Solid precipitation stage: After the coarse crushing stage is completed, maintain the constant temperature T1 for a preset time of 10min≤t4≤20min. During the constant temperature period, stir the water-material mixture at a stirring speed of 1000r / min≤r4≤3000r / min every third preset interval.

[0309] Emulsification and pulping stage: Heat to T2, where T2 is greater than T1, and intermittently stir at a stirring speed r, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is followed by a second preset interval, and the cumulative stirring time is t3, which is greater than or equal to 15 min and less than or equal to 25 min.

[0310] Optionally, the processor 101 is also used to perform: coarse crushing stage: after the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min;

[0311] Solid precipitation stage: After the coarse crushing stage is completed, maintain the constant temperature T1 for a preset time of 10min≤t1≤20min. During the constant temperature period, stir the water-material mixture at a stirring speed of 1000r / min≤r1≤3000r / min every first preset interval.

[0312] Slow boiling enrichment stage: Heat to the third temperature T2 = T boiling point - 5℃ at an average heating rate K, where K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min;

[0313] Emulsification and pulping stage: After the slow boiling and thickening stage is completed, the mixture is intermittently stirred at a stirring speed r3, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is followed by a second preset interval, and the cumulative stirring time is t3. t3 is greater than or equal to 15 min and less than or equal to 25 min. The temperature of the water-material mixture is detected within each second preset interval. When the temperature is lower than T3, heating power P2 is used to supplement the heat.

[0314] In this embodiment of the application, in response to the cooking execution command, the food processor first enters the oxygen removal stage. By heating and stirring at low speed, the pulping material is not broken. Stirring promotes the removal of oxygen from the water during the heating process and increases the concentration of ionized hydrogen ions, thereby lowering the pH and creating a weakly acidic, low-oxygen environment, which allows the seed coat of the pulping material to fully absorb water and expand. The water-material mixture is then coarsely pulverized to reduce the particle size of the pulping material, thus breaking down the nutrient cage. However, the pulping material is not completely ground to a fluid particle size, at which undesirable flavor substances are less likely to react, effectively reducing their formation. Next, the solids precipitation stage begins. The heating device is controlled by a second heating parameter to maintain the temperature of the third water-material mixture at the first temperature, and it is stirred by a third stirring parameter to promote the precipitation of solids in the material in a weakly acidic and low-oxygen environment, reducing oxidation. This reduces the oxidative loss of proteins and fats while minimizing fishy odors and increasing the soluble solids content of the finished product. Then, during the slow boiling and concentration process, the anti-protein factors are inactivated and the material is softened. Finally, the emulsification pulping stage is carried out at high temperature to complete the pulverization and promote the fusion of nutrients, and to fully emulsify the oils, thereby producing a slurry rich in nutrients, low in undesirable flavor substances, and with a good taste.

[0315] Furthermore, in response to the cooking execution command, the set pulping volume corresponding to the cooking execution command is determined. Based on the set pulping volume, the water injection device is controlled to inject water into the cooking chamber of the food processor. When the water level in the cooking chamber is detected to meet the set pulping volume, the food processor enters the oxygen removal stage. Based on the first heating parameter, the heating device is controlled to heat the first water-material mixture in the cooking chamber of the food processor, and based on the first stirring parameter, the stirring device is controlled to stir the first water-material mixture to obtain the second water-material mixture. By setting the water injection device, automatic water injection based on the set pulping volume can be achieved, thereby detecting when the water level meets the set pulping volume before entering the oxygen removal stage, improving the intelligence level of pulping.

[0316] Furthermore, in response to the cooking execution command, when the food processor enters the oxygen removal stage, the heating device is controlled to heat the first water-material mixture in the cooking chamber of the food processor at a first heating power until the temperature of the first water-material mixture reaches a second temperature, and the stirring device is controlled to stir the first water-material mixture at a first stirring speed to obtain a second water-material mixture. When the food processor enters the coarse grinding stage, the stirring device is controlled to grind the second water-material mixture at a second stirring speed for a second stirring time to obtain a third water-material mixture. When the food processor enters the solids precipitation stage, the heating device is controlled to heat the third solids mixture in the cooking chamber of the food processor at a second heating power. The water-ingredient mixture is heated to maintain the temperature of the third water-ingredient mixture at a first temperature, and the stirring device is controlled to stir the third water-ingredient mixture at a third stirring speed to obtain a fourth water-ingredient mixture. When the first temperature is maintained for a first preset duration, the food processor enters the slow boiling and thickening stage. According to the third heating parameters, the heating device is controlled to heat the fourth water-ingredient mixture in the cooking chamber of the food processor to obtain a fifth water-ingredient mixture. When the third temperature is maintained for a second preset duration, the food processor enters the emulsification and pulping stage. According to the fourth stirring parameters, the stirring device is controlled to pulverize the fifth water-ingredient mixture to form a slurry. Through the above specific parameter settings, unlike the cooking method of fully raw grinding or fully cooked grinding, the slurry production can ensure that the soluble solids, i.e., nutrients, are doubled, while reducing undesirable flavor substances in the slurry. Furthermore, from a process integration perspective, it solves the problem of easy overflow during mechanical heating in the raw grinding process, thereby producing a slurry with a richer taste.

[0317] Furthermore, the deoxygenation stage creates a low-oxygen, weakly acidic environment for the water-material mixture, which helps reduce undesirable flavor substances produced by oxidation reactions and allows the seed coat to fully absorb water and expand. Then, in the coarse grinding stage, since the seed coat has fully absorbed water and expanded, medium-speed grinding at 4000–6000 r / min breaks the material into small particles, thus destroying the nutrient cage and making it easier to release nutrients. Simultaneously, this stage maintains a low-oxygen, weakly acidic environment, preventing the release of more fishy-smelling substances due to material breakage. Next, in the slow boiling and concentration stage, the water-material mixture is heated to T2 (T2 = T boiling point - 5℃) to inactivate anti-nutritional factors such as trypsin inhibitors and lipoxygenases, and to soften the beans. Finally, high-temperature grinding completes emulsification and pulping. During this process, the motor agitates at r3 (15000 r / min ≥ r3 ≥ 10000 r / min) to complete grinding, promote nutrient fusion, and ensure thorough emulsification of oils, resulting in a smooth-textured, nutrient-rich pulp.

[0318] Furthermore, the material is initially crushed into small particles at T1 through a coarse crushing stage, breaking down the nutrient cage of the material and promoting the precipitation of solids. Then, it is slowly stirred at a constant temperature of 1000r / min≤r1≤3000r / min at T1 to promote the release of nutrients (solids) at this temperature. At the same time, the oxidation loss of proteins and fats is reduced at this temperature, ensuring a reduction in fishy substances. Then, the harmful substances (such as anti-protein factors) are inactivated through a slow boiling and concentration stage, and the material particles are fully softened by absorbing water. The high-speed grinding in the emulsification and pulping stage further promotes the precipitation of nutrients and ensures that the oils are fully emulsified, improving the nutritional value and taste of the resulting slurry.

[0319] Furthermore, the deoxygenation stage creates a low-oxygen, weakly acidic environment for the water-material mixture, which helps reduce undesirable flavor substances produced by oxidation reactions and allows the seed coat to fully absorb water and expand. Then, the mixture enters the coarse grinding stage, where the material is initially crushed into small particles at T1, breaking down the nutrient cage and promoting the precipitation of solids. Afterward, slow stirring is performed at a constant temperature of T1 at 1000 r / min ≤ r1 ≤ 3000 r / min to promote the release of nutrients (solids) at this temperature. Simultaneously, this temperature reduces the oxidative loss of proteins and fats, ensuring a reduction in fishy odors. Finally, the emulsification and pulping stage heats the water-material mixture to a high temperature of T2 and grinds it at high speed, further promoting the precipitation of nutrients and ensuring complete emulsification of oils, thus improving the nutritional value and taste of the resulting pulp.

[0320] Furthermore, the material is initially crushed into small particles at T1 through a coarse crushing stage, breaking down the nutrient cage and promoting the precipitation of solids. Then, it is slowly stirred at a constant temperature of 1000r / min≤r1≤3000r / min at T1 to promote the release of nutrients (solids) at this temperature, reduce the oxidative loss of protein and fat, and effectively deactivate endogenous oxidase activity at this temperature, thereby inhibiting the production of beany flavor. Afterward, the harmful substances (such as anti-protein factors) are inactivated through a slow boiling and concentration stage, and the material particles are fully softened by absorbing water. The high-speed grinding in the emulsification and pulping stage further promotes the precipitation of nutrients. Temperature is monitored during the stirring intervals to ensure that the oil and fat are fully emulsified at the specified temperature, thereby improving the nutritional content and taste of the resulting slurry.

[0321] It should be understood that the apparatus provided in this application embodiment is used to perform the above-described pulping control method, and therefore can achieve the same effect as the above-described implementation method.

[0322] When using an integrated unit, the device may include a processing module and a storage module. When the device is applied to a food processor, the processing module can be used to control and manage the operation of the food processor. The storage module can be used to support the food processor in executing relevant program code, etc.

[0323] The processing module may be a processor or a controller, which can implement or execute the various exemplary logic blocks, modules, and circuits described in conjunction with the disclosure of this application. The processor may also be a combination of functions that implement computing capabilities, such as a combination of one or more microprocessors, a combination of digital signal processing (DSP) and a microprocessor, etc., and the storage module may be a memory.

[0324] In addition, the device provided in this application embodiment may specifically be a chip, component or module. The chip may include a connected processor and a memory. The memory is used to store instructions. When the processor calls and executes the instructions, the chip can execute a pulping control method provided in the above embodiment.

[0325] This application also provides a computer-readable storage medium storing computer program code. When the computer program code is run on a computer, the computer executes the above-described related method steps to implement the pulping control method provided in the above embodiments.

[0326] This embodiment also provides a computer program product that, when run on a computer, causes the computer to perform the aforementioned related steps to implement the pulping control method provided in the above embodiment.

[0327] In this embodiment, the device, computer-readable storage medium, computer program product, or chip are all used to execute the corresponding methods provided above. Therefore, the beneficial effects they can achieve can be referred to the beneficial effects in the corresponding methods provided above, and will not be repeated here.

[0328] Through the above description of the embodiments, those skilled in the art will understand that, for the sake of convenience and brevity, only the division of the above functional modules is used as an example. In actual applications, the above functions can be assigned to different functional modules as needed, that is, the internal structure of the device can be divided into different functional modules to complete all or part of the functions described above.

[0329] In the embodiments provided in this application, it should be understood that the disclosed apparatus and methods can be implemented in other ways. For example, the apparatus embodiments described above are merely illustrative; for instance, the division of modules or units is only a logical functional division, and in actual implementation, there may be other division methods. For example, multiple units or components may be combined or integrated into another device, or some features may be ignored or not executed. Furthermore, the coupling or direct coupling or communication connection shown or discussed may be through some interfaces; the indirect coupling or communication connection between devices or units may be electrical, mechanical, or other forms.

[0330] The above description is merely a specific embodiment of this application, but the scope of protection of this application is not limited thereto. Any variations or substitutions that can be easily conceived by those skilled in the art within the scope of the technology disclosed in this application should be included within the scope of protection of this application. Therefore, the scope of protection of this application should be determined by the scope of the claims.

Claims

1. A pulping control method, characterized in that, Applied to a food processor, the food processor including a blending device and a heating device, the method includes: In response to the cooking execution command, when the food processor enters the oxygen removal stage, the heating device is controlled to heat the first water-material mixture in the cooking chamber of the food processor according to the first heating parameter, and the stirring device is controlled to stir the first water-material mixture according to the first stirring parameter to obtain a second water-material mixture. When the food processor enters the coarse grinding stage, the mixing device is controlled according to the second mixing parameters to grind the second water-material mixture to obtain a third water-material mixture; the average particle size of the material particles in the third water-material mixture is smaller than the average particle size of the material particles in the second water-material mixture; When the food processor enters the solids precipitation stage, the heating device is controlled according to the second heating parameter to maintain the temperature of the third water-material mixture at the first temperature, and the stirring device is controlled according to the third stirring parameter to stir the third water-material mixture to obtain the fourth water-material mixture. When the food processor enters the slow boiling and thickening stage, the heating device is controlled to heat the fourth water-material mixture according to the third heating parameter to obtain the fifth water-material mixture; When the food processor enters the emulsification and pulping stage, the stirring device is controlled according to the fourth stirring parameter to pulverize the fifth water-material mixture so that the fifth water-material mixture forms a slurry.

2. The method according to claim 1, characterized in that, The food processor also includes a water injection device; In response to a cooking execution command, when the food processor enters the oxygen degassing stage, the heating device is controlled according to a first heating parameter to heat the first water-material mixture in the cooking chamber of the food processor, and the stirring device is controlled according to a first stirring parameter to stir the first water-material mixture to obtain a second water-material mixture, comprising: In response to a cooking execution command, determine the set pulping amount corresponding to the cooking execution command; The water injection device is controlled to inject water into the cooking chamber of the food processor according to the set pulping volume; Once the water level in the cooking chamber is detected to meet the set pulping volume, the food processor is determined to enter the oxygen removal stage. The heating device is controlled to heat the first water-material mixture in the cooking chamber of the food processor according to the first heating parameter, and the stirring device is controlled to stir the first water-material mixture according to the first stirring parameter to obtain the second water-material mixture.

3. The method according to claim 1, characterized in that, The step of controlling the heating device to heat the first water-material mixture in the cooking chamber of the food processor according to the first heating parameter includes: The heating device is controlled to heat the first water-ingredient mixture in the cooking chamber of the food processor with a first heating power until the temperature of the first water-ingredient mixture reaches a second temperature.

4. The method according to claim 3, characterized in that, The first heating power P1 satisfies that P1 is greater than or equal to 1000W and less than or equal to 1200W, and the second temperature T1 satisfies that T1 is greater than or equal to 78°C and less than or equal to 82°C.

5. The method according to claim 1, characterized in that, The step of controlling the stirring device to stir the first water-material mixture according to the first stirring parameters includes: The stirring device is controlled to stir the first water-material mixture at a first stirring speed.

6. The method as described in claim 5, characterized in that, The control of the stirring device to stir the first water-material mixture at a first stirring speed includes: At each first preset interval, the stirring device is controlled to stir the first water-material mixture at a first stirring speed for a first stirring duration.

7. The method according to any one of claims 5 or 6, characterized in that, The first stirring speed is the minimum speed allowed by the motor of the stirring device.

8. The method according to claim 7, characterized in that, The minimum permissible speed of the motor is greater than 1000 r / min and less than 3000 r / min.

9. The method according to claim 6, characterized in that, The first preset interval duration t1 satisfies that t1 is greater than or equal to 50s and less than or equal to 70s, and the first stirring duration t2 satisfies that t2 is greater than 0s and less than or equal to 6s.

10. The method according to claim 1, characterized in that, When the food processor enters the coarse grinding stage, the mixing device is controlled according to the second mixing parameters to grind the second water-material mixture to obtain a third water-material mixture, including: When the food processor enters the coarse grinding stage, the stirring device is controlled to grind the second water-material mixture at a second stirring speed for a second stirring time to obtain a third water-material mixture.

11. The method according to claim 10, characterized in that, The second stirring speed r2 satisfies that r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and the second stirring duration t3 is greater than or equal to 0.5 min and less than or equal to 1.5 min.

12. The method according to claim 1, characterized in that, When the food processor enters the solids separation stage, controlling the heating device to maintain the temperature of the third water-material mixture at a first temperature according to the second heating parameter includes: When the food processor enters the solids precipitation stage, the heating device is controlled to heat the third water-material mixture in the cooking chamber of the food processor with a second heating power so that the temperature of the third water-material mixture is maintained at the first temperature.

13. The method according to claim 1, characterized in that, The step of controlling the stirring device to stir the third water-material mixture according to the third stirring parameters includes: The stirring device is controlled to stir the third water-material mixture at a third stirring speed.

14. The method according to claim 13, characterized in that, The control of the stirring device to stir the third water-material mixture at a third stirring speed includes: At each second preset interval, the stirring device is controlled to stir the third water-material mixture at a third stirring speed for a third stirring duration.

15. The method according to claim 13, characterized in that, The second preset interval duration t4 satisfies that t4 is greater than or equal to 25s and less than or equal to 35s, the third stirring speed r3 satisfies that r3 is greater than 1000r / min and less than 3000r / min, and the third stirring duration t5 satisfies that t5 is greater than 0s and less than or equal to 6s.

16. The method according to claim 1, characterized in that, When the food processor enters the slow boiling and thickening stage, the heating device is controlled according to the third heating parameter to heat the fourth water-material mixture in the cooking chamber of the food processor to obtain the fifth water-material mixture, including: When the first temperature is maintained for a first preset duration, the food processor is determined to enter the slow boiling and thickening stage. The heating device is controlled according to the third heating parameter to heat the fourth water-material mixture in the cooking chamber of the food processor to obtain the fifth water-material mixture.

17. The method according to claim 1 or 16, characterized in that, When the food processor enters the slow boiling and thickening stage, the heating device is controlled according to the third heating parameter to heat the fourth water-material mixture to obtain the fifth water-material mixture, including: When the food processor enters the slow boiling and thickening stage, the heating device is controlled to heat the fourth water-ingredient mixture at a preset heating rate until the temperature of the fourth water-ingredient mixture reaches the third temperature, so as to obtain the fifth water-ingredient mixture.

18. The method according to claim 17, characterized in that, The preset heating rate K satisfies that K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min.

19. The method according to claim 1, characterized in that, When the food processor enters the emulsification and slurry-making stage, the stirring device is controlled according to the fourth stirring parameter to pulverize the fifth water-material mixture so that the fifth water-material mixture forms a slurry, including: When the third temperature is maintained for a second preset duration, the food processor is determined to enter the emulsification and pulping stage. The stirring device is controlled according to the fourth stirring parameter to pulverize the fifth water-material mixture so that the fifth water-material mixture forms a slurry.

20. The method according to claim 1 or 19, characterized in that, The step of controlling the stirring device to pulverize the fifth water-material mixture according to the fourth stirring parameter to form a slurry includes: Every third preset interval, the stirring device is controlled to crush the fifth water-material mixture at a fourth stirring speed for a fourth stirring time, until the cumulative stirring time reaches the fifth stirring time.

21. The method according to claim 20, characterized in that, The fourth stirring speed r4 satisfies that r4 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min, and the fifth stirring time t6 satisfies that t6 is greater than or equal to 15 min and less than or equal to 25 min.

22. The method according to claim 20, characterized in that, The method further includes: The temperature of the fifth water-material mixture is detected within each of the third intervals. When the temperature is lower than the fourth temperature, the heating device is controlled to heat the fifth water-material mixture according to the fourth heating parameter so that the temperature of the fifth water-material mixture reaches the fourth temperature.

23. The method according to claim 20, characterized in that, When the temperature is lower than the fourth temperature, controlling the heating device to heat the fifth water-material mixture according to the fourth heating parameter to bring the temperature of the fifth water-material mixture to the fourth temperature includes: When the temperature is lower than the fourth temperature, the heating device is controlled to heat the fourth water-material mixture with a third heating power until the temperature of the fourth water-material mixture reaches the fourth temperature.

24. A pulping control method, characterized in that, Applied to a food processor, the method includes: Aeration stage: The water-material mixture is heated to temperature T1 with heating power P1, wherein T1 is greater than or equal to 78℃ and less than or equal to 82℃, P1 is greater than or equal to 1000w and less than or equal to 1200w, and the water-material mixture is stirred without pulverization at a first stirring speed r1 and a first stirring time at a first preset interval, wherein r1 is greater than or equal to 1000r / min and less than or equal to 3000r / min; Coarse crushing stage: After the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min. Slow boiling enrichment stage: Heat to the third temperature T2 = T boiling point - 5℃ at an average heating rate K, where K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min; Emulsification and pulping stage: After the slow boiling and thickening stage is completed, the mixture is intermittently stirred at a stirring speed r3, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is followed by a second preset interval, and the cumulative stirring time is t3, which is greater than or equal to 15 min and less than or equal to 25 min.

25. A pulping control method, characterized in that, Applied to a food processor, the method includes: Coarse crushing stage: After the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min. Solid precipitation stage: After the coarse crushing stage is completed, the temperature is kept constant for a preset time of 10min≤t1≤20min. During the constant temperature period, the water-material mixture is stirred at a stirring speed of 1000r / min≤r1≤3000r / min every first preset interval. Slow boiling enrichment stage: Heat to the third temperature T2 = T boiling point - 5℃ at an average heating rate K, where K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min; Emulsification and pulping stage: After the slow boiling and thickening stage is completed, the mixture is intermittently stirred at a stirring speed r3, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is followed by a second preset interval, and the cumulative stirring time is t3, which is greater than or equal to 15 min and less than or equal to 25 min.

26. A pulping control method, characterized in that, Applied to a food processor, the method includes: Aeration stage: The water-material mixture is heated to temperature T1 with heating power P1, wherein T1 is greater than or equal to 78℃ and less than or equal to 82℃, P1 is greater than or equal to 1000w and less than or equal to 1200w, and the water-material mixture is stirred without pulverization at a first stirring speed r1 and a first stirring time at a first preset interval, wherein r1 is greater than or equal to 1000r / min and less than or equal to 3000r / min; Coarse crushing stage: After the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min. Solid precipitation stage: After the coarse crushing stage is completed, the constant temperature T1 is maintained for a preset time of 10min≤t4≤20min. During the constant temperature period, the water-material mixture is stirred at a stirring speed of 1000r / min≤r4≤3000r / min every third preset interval. Emulsification and pulping stage: heating to T2, where T2 is greater than T1, intermittently stirring at a stirring speed r, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min, with a second preset interval between each third stirring time, and a cumulative stirring time t3, where t3 satisfies greater than or equal to 15 min and less than or equal to 25 min.

27. A pulping control method, characterized in that, Applied to a food processor, the method includes: Coarse crushing stage: After the temperature reaches T1, the water-material mixture is stirred at a stirring speed r2 for a second stirring time t2, so that the initial particles in the water-material mixture are cut into block particles smaller than the initial particles, wherein r2 is greater than or equal to 4000 r / min and less than or equal to 6000 r / min, and t2 is greater than or equal to 0.5 min and less than or equal to 1.5 min. Solid precipitation stage: After the coarse crushing stage is completed, the temperature is kept constant for a preset time of 10min≤t1≤20min. During the constant temperature period, the water-material mixture is stirred at a stirring speed of 1000r / min≤r1≤3000r / min every first preset interval. Slow boiling enrichment stage: Heat to the third temperature T2 = T boiling point - 5℃ at an average heating rate K, where K is greater than or equal to 1.2℃ / min and less than or equal to 2.0℃ / min; Emulsification and pulping stage: After the slow boiling and thickening stage is completed, the mixture is intermittently stirred at a stirring speed r3, where r3 is greater than or equal to 10000 r / min and less than or equal to 15000 r / min. The third stirring time is followed by a second preset interval, and the cumulative stirring time is t3, which is greater than or equal to 15 min and less than or equal to 25 min. The temperature of the water-material mixture is detected within each second preset interval. When the temperature is lower than T3, heating power P2 is used to supplement the heat.

28. A pulping control device, the device comprising: A first control unit is configured to respond to a cooking execution command, and when the food processor enters the oxygen removal stage, control the heating device to heat the first water-material mixture in the cooking chamber of the food processor according to a first heating parameter, and control the stirring device to stir the first water-material mixture according to a first stirring parameter to obtain a second water-material mixture. The second control unit is used to control the stirring device to crush the second water-material mixture according to the second stirring parameters when the food processor enters the coarse crushing stage, so as to obtain a third water-material mixture; the average particle size of the material particles in the third water-material mixture is smaller than the average particle size of the material particles in the second water-material mixture. The third control unit is used to control the heating device to maintain the temperature of the third water-material mixture at a first temperature according to the second heating parameter when the food processor enters the solid precipitation stage, and to control the stirring device to stir the third water-material mixture according to the third stirring parameter to obtain a fourth water-material mixture. The fourth control unit is used to control the heating device to heat the fourth water-material mixture according to the third heating parameter when the food processor enters the slow boiling and thickening stage, so as to obtain the fifth water-material mixture; The fifth control unit is used to control the stirring device to pulverize the fifth water-material mixture according to the fourth stirring parameter when the food processor enters the emulsification and pulping stage, so as to form a slurry from the fifth water-material mixture.

29. A food processor, characterized in that, The food processor includes: Memory, used to store executable program code; A processor for calling and running the executable program code from the memory, causing the food processor to perform the method as described in any one of claims 1 to 27.

30. A computer-readable storage medium, characterized in that, The computer-readable storage medium stores computer program code that, when executed, implements the method as described in any one of claims 1 to 27.

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