Preparation method for hydrosol solution

Abstract

Disclosed in the present invention is a preparation method for a hydrosol solution. The preparation method comprises the following steps: classifying, according to material characters, all materials required for hydrosol solution preparation, and, according to the material characters, separately allocating the classified materials into feeding stations of a hydrosol solution preparation system for later use; turning on a heating system of the hydrosol solution preparation system to pre-heat a processing pipeline of a mixing and shearing apparatus, such that the temperature in the processing pipeline meets a hydrosol solution processing requirement; calculating and configuring a flow velocity for the materials of each material character to enter the processing pipeline; and starting the mixing and shearing apparatus of the hydrosol solution preparation system, and synchronously opening each feeding station, each type of materials being conveyed into the processing pipeline according to the configured flow velocity, and a first screw in the processing pipeline mixing and shearing all the materials at the same time, so as to obtain a uniform hydrosol solution. The present invention can reduce the working intensity of operators, and involves a simple preparation process and achieves high continuity, reducing the time consumed by the whole process.

Description

TECHNICAL FIELD The present invention relates to the field of hydrosol solution processing, and in particular, to a preparation method for a hydrosol solution. BACKGROUND As a highly hydrophilic polymer material, water-soluble colloid can dissolve or swell in water to form a relatively viscous aqueous solution or dispersion system, and the aqueous solution and dispersion system are commonly referred to as a polymer aqueous solution or a hydrosol solution. Hydrophilic groups in the water-soluble colloid not only make it water soluble, but also have chemical functions, as well as various physical functions such as dispersion, flocculation, viscosity enhancement, drag reduction, adhesion, film formation, gelation, and chelation. Therefore, the water-soluble colloid is widely used in daily chemicals, food, and pharmaceutical industries. Since polymer compounds have structural complexity such as large molecular weights and poly dispersity, the dissolution phenomena thereof are much more complex than those of smallmolecule substances. Polymers and solvent molecules have a significant difference in dimensions as well as a great difference in molecular motion velocities. The solvent molecules can penetrate into high polymers relatively quickly, while the diffusion of the polymers into solvents is very slow. In this way, a dissolution procedure of the high polymers goes through two stages: first, the solvent molecules penetrate into the interior of the high polymers, causing the volumes of the high polymers to expand, which is referred to as “swelling”; and then, the polymers are uniformly dispersed in the solvent to form a completely-dissolved homogeneous system with molecules dispersed. The whole dissolution procedure is carried out over a long period of time, usually accompanied by stirring, shear homogenization, and other conditions. Meanwhile, to accelerate the dissolution of certain polymer colloid, the dissolution procedure needs to be carried out at higher temperatures. The water-soluble colloid is widely used in food and plays an important role as an indispensable part of ingredients in some types of food. For example, for gel jelly products, gummy candy products, soft capsules, and the like in the food industry, the water-soluble colloid needs to be used and prepared into a hydrosol solution so as to obtain a final product. An existing preparation process for a hydrosol solution, for example, a process for preparing a hydrosol solution of gel gummy candies, includes the following preparation procedure: sugar melting: adding white granulated sugar, glucose syrup, and water into a sugar melting tank for dilution; colloid dissolution: conveying a diluted solution into a colloid tank and adding vegetable gum and a large amount of water to perform high-temperature colloid dissolution; sugar boiling: after the colloid dissolution, transferring the solution to a sugar boiling tank for boiling, and filtering out water to obtain syrup; temporary storage: conveying obtained syrup into a temporary storage tank for temporary storage; and sugar solution preparation: conveying a sugar solution in the temporary storage tank into a functional mixing tank, and adding required functional components to obtain a required hydrosol solution for the gel gummy candies. The aforementioned hydrosol solution process requires operation modes of sugar melting, colloid dissolution, sugar boiling, and functional stirring and mixing, and requires multiple persons to carry out the preparation procedure step by step based on the preparation process, resulting in high working intensity of operators, cumbersome manufacturing procedure, and poor continuity. The whole preparation procedure takes 4-5 hours, resulting in high time consumption of the whole procedure and high production costs. SUMMARY In view of the deficiencies of the prior art, the present invention provides a preparation method for a hydrosol solution. By adopting the preparation method, the working intensity of operators can be reduced, a simple manufacturing procedure and high continuity are achieved, and the time consumed by the whole procedure is reduced. The present invention is achieved by the following technical solution: A preparation method for a hydrosol solution, including the following steps: classifying total materials required for hydrosol solution preparation according to material properties, and separately allocating classified materials to each of feeding stations of a hydrosol solution preparation system for later use according to the material properties; switching on a heating system of the hydrosol solution preparation system to preheat a processing pipeline of a mixing and shearing device, allowing temperature inside the processing pipeline to meet processing requirements of the hydrosol solution; calculating and configuring a flow rate of the materials with each material property entering the processing pipeline; and starting the mixing and shearing device of the hydrosol solution preparation system, synchronously opening each of the feeding stations, conveying each material into the processing pipeline according to a configured flow rate, and simultaneously mixing and shearing all the materials by a first screw in the processing pipeline to obtain a homogeneous hydrosol solution. Further, the step of classifying total materials required for hydrosol solution preparation according to material properties, and separately allocating classified materials to each of feeding stations of a hydrosol solution preparation system for later use according to the material properties specifically includes the following steps: classifying the total materials required for the hydrosol solution preparation into a solid phase material, an aqueous phase material, an aqueous phase functional material, an oil phase functional material, and other ingredients according to the material properties; simultaneously allocating the solid phase material to a first feeding unit, allocating the aqueous phase material to a second feeding unit, allocating the aqueous phase functional material to a third feeding unit, allocating the oil phase functional material to a fourth feeding unit, and allocating the other ingredients to a fifth feeding unit; and performing temperature control on each feeding unit according to the material properties of each material for later use. Further, the step of starting the mixing and shearing device of the hydrosol solution preparation system, synchronously opening each of the feeding stations, conveying each material into the processing pipeline according to a configured flow rate, and simultaneously mixing and shearing all the materials by a first screw in the processing pipeline to obtain a homogeneous hydrosol solution specifically includes the following steps: starting the mixing and shearing device of the hydrosol solution preparation system, and synchronously opening each of the feeding stations; enabling the solid phase material and the aqueous phase material to enter the processing pipeline from an upstream end of the processing pipeline, and preliminarily shearing and mixing the solid phase material and the aqueous phase material under an action of the first screw and then conveying to a downstream end of the processing pipeline; enabling the aqueous phase functional material, the oil phase functional material, and the other ingredients to enter the processing pipeline from the downstream end of the processing pipeline, preliminarily mixing the aqueous phase functional material, the oil phase functional material, and the other ingredients with a mixture of the solid phase material and the aqueous phase material at the upstream end, and further conveying towards a discharge port; shearing and mixing the aqueous phase functional material, the oil phase functional material, and the other ingredients with the mixture of the solid phase material and the aqueous phase material again, and then discharging from the processing pipeline; and obtaining the homogeneous hydrosol solution at the discharge port of the processing pipeline. Further, the step of starting the mixing and shearing device of the hydrosol solution preparation system, synchronously opening each of the feeding stations, conveying each material into the processing pipeline according to a configured flow rate, and simultaneously mixing and shearing all the materials by a first screw in the processing pipeline to obtain a homogeneous hydrosol solution further includes the following steps: discarding the solid phase material, the aqueous phase material, the aqueous phase functional material, the oil phase functional material, and the other ingredients that are not fully and evenly mixed in the processing pipeline in an early working stage of the mixing and shearing device. Further, the step of calculating and configuring a flow rate of the materials with each material property entering the processing pipeline specifically includes: calculating the flow rate of the materials with each material property entering the processing pipeline; and allocating a calculated flow rate value of the materials with each material property to each of the feeding stations. Further, the step of calculating the flow rate of the materials with each material property entering the processing pipeline specifically includes: defining a discharging flow rate of the discharge port of the processing pipeline as Fout, where a range of Fout is 50-300 kg / h; the flow rate of each material entering the processing pipeline meeting the following conditions: Fb=FOutxb; Fc Foutxc, Fd=F0Utxd; and Fe=FOutxe; where Fa, Fb, Fc, Fa, and Fe are the flow rates of the solid phase material, the aqueous phase material, the aqueous phase functional material, the oil phase functional material, and the other ingredients entering the processing pipeline, respectively; and a, b, c, d, and e are mass proportions of the solid phase material, the aqueous phase material, the aqueous phase functional material, the oil phase functional material, and the other ingredients in the total materials, respectively. Further, the step of switching on a heating system of the hydrosol solution preparation system to preheat a processing pipeline of a mixing and shearing device, allowing temperature inside the processing pipeline to meet processing requirements of the hydrosol solution specifically includes: switching on an electromagnetic infrared heater to preheat the processing pipeline of the mixing and shearing device; determining whether the temperature inside the processing pipeline meets the processing requirements of the hydrosol solution in real time by a first temperature sensor; continuously heating the processing pipeline of the mixing and shearing device by the electromagnetic infrared heater if the first temperature sensor detects that a temperature value is less than a preset minimum value; stopping heating if the first temperature sensor detects that the temperature value is greater than a preset maximum value; and controlling the temperature inside the processing pipeline to be within a temperature range required for processing of the hydrosol solution. A preparation system based on the preparation method for a hydrosol solution described above, including: a mixing and shearing device; a controller; and a plurality of feeding stations, configured to store materials with different material properties, respectively; where the plurality of feeding stations are all connected to the mixing and shearing device to convey the materials with different material properties into the mixing and shearing device, the controller is electrically connected to the plurality of feeding stations to control material conveying rates of the plurality of feeding stations, respectively, and the controller is electrically connected to the mixing and shearing device to control the mixing and shearing device to mix and shear the materials with different material properties. Further, the mixing and shearing device includes a processing pipeline, a first screw, and a drive motor, the feeding stations are in communication with the processing pipeline to convey the materials with different material properties into the processing pipeline, the first screw is arranged inside the processing pipeline, the drive motor is electrically connected to the controller to drive the first screw to mix and shear the materials in the processing pipeline so as to obtain the hydrosol solution, and the first screw discharges an obtained hydrosol solution from a discharge port of the processing pipeline. Further, the plurality of feeding stations include a first feeding unit for storing a solid phase material, a second feeding unit for storing an aqueous phase material, a third feeding unit for storing an aqueous phase functional material, a fourth feeding unit for storing an oil phase functional material, and a fifth feeding unit for storing other ingredients, and the first feeding unit, the second feeding unit, the third feeding unit, the fourth feeding unit, and the fifth feeding unit are all in communication with the processing pipeline through a pipeline. Compared to the prior art, the present invention has the following advantages: 1. The system and preparation method can be applied to the preparation procedure of hydrosol solutions in daily chemicals, food, and drugs, and can simultaneously introduce various functional components and auxiliary materials online. Especially, they have more advantages in the preparation of relatively viscous water-soluble systems such as gel jelly solutions, soft capsule rubber solutions, and gummy candy syrup. 2. The process and system also have unique advantages in the aspect of thermosensitive functional materials. The first feeding unit for storing the solid phase material and the second feeding unit for storing the aqueous phase material are connected to one side of the processing pipeline close to the drive motor, and after the materials entering an online material mixing and shearing device are fully dispersed, dissolved, and sheared, the third feeding unit and the fourth feeding unit for storing the functional materials and the fifth feeding unit for storing the other ingredients are connected near an outlet end of the processing pipeline. Therefore, the time for heating, mixing, and shearing of the functional materials is reduced, the stability of the functional components is greatly improved, the loss of nutrients is reduced, and higher functional content and better quality of the obtained hydrosol solution are achieved. 3. Compared to a conventional hydrosol solution preparation process, this process changes the procedure of gradually feeding, mixing, and boiling, adopts a material mixing and shearing device and a quantitative feeding system to cascade the hydrosol solution preparation procedure, and digitally and automatically adjusts a discharging rate based on proportions of the materials in a formula. Therefore, the hydrosol solution preparation procedure is simplified, data of the hydrosol solution preparation procedure is clearer, adjustment modes are more controllable, and time and labor costs are saved. Compared to batch production, this process can achieve continuous production of the hydrosol solution during preparation, thereby further reducing production costs and improving labor efficiency. 4. The system and process require a short time for hydrosol solution preparation, and only take the time to pass through the online material mixing and shearing device from the feeding of each material to the final hydrosol solution preparation. Therefore, the time consumed by the whole procedure is reduced, and the total time for the hydrosol solution preparation does not exceed 3 min, which greatly improves the production efficiency. 5. The working intensity of operators is reduced, a simple manufacturing procedure and high continuity are achieved, the occupation of factory space is reduced, and the economic benefits are improved. BRIEF DESCRIPTION OF THE DRAWINGS FIG. lisa schematic structural diagram of a preparation system for a hydrosol solution according to an embodiment of the present invention; FIG. 2 is a schematic structural diagram of a thermal insulation pipeline; FIG. 3 is a schematic structural diagram of a first screw; FIG. 4 is a control block diagram of a preparation system for a hydrosol solution; and FIG. 5 is a flowchart of a preparation method for a hydrosol solution. 100. Mixing and shearing device; 101. processing pipeline; 110. discharge port; 111. first feed inlet; 112. second feed inlet; 113. third feed inlet; 114. fourth feed inlet; 115. fifth feed inlet; 102. first screw; 121. propulsion section; 122. shearing section; 123. propulsion thread module; 124. shearing thread module; 103. drive motor; 104. electromagnetic infrared heater; 105. thermal insulation sleeve; 106. pressure sensor; 107. first temperature sensor; 108. second temperature sensor; 109. frequency converter; 200. controller; 300. feeding station; 1. first feeding unit; 10. hopper; 11. second propulsion screw; 12. solid material pipeline; 13. servo motor; 2. second feeding unit; 20. second batching tank; 21. second metering pump; 3. third feeding unit; 30. third batching tank; 31. third metering pump; 4. fourth feeding unit; 40. fourth batching tank; 41. fourth metering pump; 5. fifth feeding unit; 50. fifth batching tank; 51. fifth metering pump; 6. stirring apparatus; 60. stirring motor; 61. stirring rod; 7. tank sleeve; 70. third temperature sensor; 400. pipeline; 401. pipe sleeve; 402. thermal insulation chamber; 403. hot water tank; 404. hot water pump; 500. bottom plate; 501. base; 502. mounting plate; 503. first support frame; 504. second support frame; 505. support plate; 600. man-machine interface. DETAILED DESCRIPTION OF THE EMBODIMENTS The following provides a further non-restrictive detailed description for the technical solution of the present invention in conjunction with preferred embodiments and accompanying drawings thereof. In the description of the present invention, it should be understood that the orientations or positional relationships indicated by the terms "center", "longitudinal", "transverse", "length", "width", "thickness", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside", "outside", "clockwise", "counter-clockwise", "axial", "radial", "circumferential", and the like are in accordance with those shown in the accompanying drawings. In addition, the terms "first" and "second" are merely intended for a purpose of description, and shall not be understood as an indication or implication of relative importance or an implicit indication of the number of the indicated technical features. Therefore, features defined by "first" and "second" can explicitly or implicitly include at least one of such features. In the description of the present invention, "a plurality of refers to at least two, for example, two or three, unless otherwise specifically defined. The embodiments described below with reference to the accompanying drawings are exemplary and are intended to explain the present invention, but shall not be understood as a limitation on the present invention. As shown in FIG. 1 to FIG. 4, a preparation system for a hydrosol solution according to an embodiment of the present invention includes a mixing and shearing device 100, a controller 200, a plurality of feeding stations 300, and a man-machine interface 600. The feeding stations 300 are connected to the mixing and shearing device 100 through a pipeline 400 and convey materials with different material properties into the mixing and shearing device 100, the controller 200 is electrically connected to the plurality of feeding stations 300 and controls material conveying rates of each feeding station 300, the controller 200 is electrically connected to the mixing and shearing device 100 and controls operation of the mixing and shearing device 100, the mixing and shearing device 100 is configured to simultaneously mix and shear the materials with different material properties to obtain the hydrosol solution, the hydrosol solution is discharged from the mixing and shearing device 100 after being processed, and the man-machine interface 600 is electrically connected to the controller 200 to issue work instructions and display various system parameters. The mixing and shearing device 100 includes a processing pipeline 101, a first screw 102, a drive motor 103, and an electromagnetic infrared heater 104. The feeding stations 300 are in communication with the processing pipeline 101 to convey the materials with different material properties into the processing pipeline 101, the electromagnetic infrared heater 104 is arranged at an outer side of the processing pipeline 101 and is electrically connected to the controller 200, a thermal insulation sleeve 105 is arranged at an outer side of the electromagnetic infrared heater 104, the first screw 102 is arranged inside the processing pipeline 101, the drive motor 103 is fixedly connected to the first screw 102, and the drive motor 103 is electrically connected to the controller 200 to drive the first screw 102 to simultaneously mix and shear all the materials in the processing pipeline 101 so as to obtain the hydrosol solution, and the first screw 102 discharges an obtained hydrosol solution from a discharge port 110 of the processing pipeline 101. The mixing and shearing device 100 further includes a bottom plate 500, and the processing pipeline 101 and the drive motor 103 are fixedly arranged on the bottom plate 500. The bottom plate 500 includes a base 501 as well as a mounting plate 502 and a first support frame 503 that are fixed on the base 501. The processing pipeline 101 is fixed above the first support frame 503, the drive motor 103 is fixed on the mounting plate 502, and a motor shaft (not shown in the figure) of the drive motor 103 passes through the first support frame 503 to drive the first screw 102 to rotate. A second support frame 504 and a support plate 505 are further fixed on the mounting plate 502, the second support frame 504 is fixedly connected to a solid material pipeline 12, and the support plate 505 is fixedly connected to a servo motor 13. A second feeding unit 2, a third feeding unit 3, a fourth feeding unit 4, and a fifth feeding unit 5 are all fixed above the processing pipeline 101 through mounting racks (not shown in the figure). Specifically, the controller 200 controls working of the drive motor 103 through a frequency converter 109. A pressure sensor 106 is arranged at the discharge port 110, and the pressure sensor 106 is electrically connected to the controller 200. When the pressure sensor 106 detects that a pressure value at the discharge port 110 is greater than a set threshold, a signal is fed back to the controller 200. The controller 200 controls the drive motor 103 to reduce a rotational speed, otherwise, increases the rotational speed of the drive motor 103. A first temperature sensor 107 is arranged inside the processing pipeline 101 to monitor the temperature of the materials in the processing pipeline 101, a second temperature sensor 108 is arranged inside the thermal insulation sleeve 105, and both the first temperature sensor 107 and the second temperature sensor 108 are connected to the controller 200. When the first temperature sensor 107 / the second temperature sensor 108 detects that a temperature is less than a preset temperature, the controller 200 controls the electromagnetic infrared heater 104 to work; otherwise, the electromagnetic infrared heater 104 is stopped to maintain that the temperature inside the processing pipeline 101 is controlled to be within a temperature range required for processing of the hydrosol solution. In addition, the electromagnetic infrared heater 104 can also be controlled by the controller 200 to continuously heat the processing pipeline 101. The first temperature sensor 107 and the second temperature sensor 108 are used to monitor whether the temperature inside the processing pipeline 101 and the thermal insulation sleeve 105 meets working requirements, respectively. The processing pipeline 101 is provided with a plurality of feed inlets, and the number of the feed inlets is consistent with that of the feeding stations 300, ensuring that each of the feeding stations 300 is connected to one of the feed inlets. In this embodiment, five feed inlets are arranged, namely a first feed inlet 111, a second feed inlet 112, a third feed inlet 113, a fourth feed inlet 114, and a fifth feed inlet 115. The first feed inlet 111 and the second feed inlet 112 are adjacently arranged at one end of the processing pipeline 101 close to the drive motor 103, and the third feed inlet 113, the fourth feed inlet 114, and the fifth feed inlet 115 are adjacently arranged at one end of the processing pipeline 101 close to the discharge port 110 (i.e., one end of the processing pipeline 101 away from the drive motor 103). Due to large proportions of a solid phase material and an aqueous phase material in the materials required for the hydrosol solution, the first feed inlet 111 and the second feed inlet 112 respectively corresponding to a first feeding unit 1 for storing the solid phase material and the second feeding unit 2 for storing the aqueous phase material are adjacently arranged at one end of the processing pipeline 101 close to the drive motor 103, in order to ensure that the solid phase material and the aqueous phase material can be sheared for a sufficient time in the processing pipeline 101, thus achieving a purpose of sufficient shearing. After sufficient shearing, the solid phase material and the aqueous phase material are sheared and mixed again with small proportions of an aqueous phase functional material, an oil phase functional material, and other ingredients. The device is scientific and reasonable in design, thereby saving unnecessary energy consumption. In this embodiment, a twin-screw mixing and shearing device is used, two identical first screws 102 are used to cooperate and work together to mix and shear the materials in the processing pipeline 101. The first screw 102 has a diameter of 75 mm, and the first screw 102 includes a plurality of sets of propulsion sections 121 and shearing sections 122. The propulsion sections 121 and the shearing sections 122 are arranged at intervals from each other. Moreover, the propulsion section 121 is composed of a plurality of sets of propulsion thread modules 123, and the shearing section 122 is composed of a plurality of sets of shearing thread modules 124. The first feed inlet 111, the second feed inlet 112, the third feed inlet 113, the fourth feed inlet 114, and the fifth feed inlet 115 all correspond to positions of the propulsion sections 121 in the processing pipeline 101. Moreover, the first feed inlet 111 and the second feed inlet 112 correspond to the same segment of the propulsion section 121 in the processing pipeline 101, and the third feed inlet 113, the fourth feed inlet 114, and the fifth feed inlet 115 correspond to the same segment of the propulsion section 121 in the processing pipeline 101. Further, a portion of the first screw 102 located between the second feed inlet 112 (the first feed inlet 111) and the third feed inlet 113 (the fourth feed inlet 114 / the fifth feed inlet 115) is provided with at least one set of shearing sections 122, and a portion of the first screw 102 located between the third feed inlet 113 (the fourth feed inlet 114 / the fifth feed inlet 115) and the discharge port 110 is provided with at least one set of shearing sections 122. That is, the materials entering from each feed inlet are first preliminarily mixed and pushed to the shearing section 122 by the propulsion section 121, and then different materials are fully sheared and mixed by the shearing section 122. The first screws are arranged at intervals from each other through the propulsion section 121 and the shearing section 122, and different materials can be mixed extremely quickly by the propulsion section 121 and sheared by the shearing section 122. A thread pitch of the propulsion thread module 123 of the propulsion section 121 is large, and a distance that the materials are pushed to travel per unit time is long, which improves the processing efficiency of the materials. A thread pitch dl of the propulsion thread module 123 of the propulsion section 121 is 36-112 mm, and a thread pitch d2 of the shearing thread module 124 of the shearing section 122 is 22-96 mm. In this embodiment, the thread pitch dl of the propulsion thread module 123 of the propulsion section 121 is specifically 72 mm, a cumulative total length of the propulsion section 121 is 216 mm, the thread pitch d2 of the shearing thread module 124 of the shearing section 122 is specifically 56 mm, and a cumulative total length of the shearing section is 168 mm. In this embodiment, PLC S7-1200 is selected as the controller 200. The feeding station 300 includes the first feeding unit 1 for storing the solid phase material, the second feeding unit 2 for storing the aqueous phase material, the third feeding unit 3 for storing the aqueous phase functional material, the fourth feeding unit 4 for storing the oil phase functional material, and the fifth feeding unit 5 for storing the other ingredients. The first feeding unit 1, the second feeding unit 2, the third feeding unit 3, the fourth feeding unit 4, and the fifth feeding unit 5 are all in communication with the processing pipeline 101 through the pipeline 400. Specifically, the first feeding unit 1 is connected to the first feed inlet 111 in the processing pipeline 101, the second feeding unit 2 is connected to the second feed inlet 112 in the processing pipeline 101, the third feeding unit 3 is connected to the third feed inlet 113 in the processing pipeline 101, the fourth feeding unit 4 is connected to the fourth feed inlet 114 in the processing pipeline 101, and the fifth feeding unit 5 is connected to the fifth feed inlet 115 in the processing pipeline 101. The first feeding unit 1 includes a hopper 10 for storing the solid phase material, a second propulsion screw 11, the solid material pipeline 12, and a servo motor 13. One side of the solid material pipeline 12 is connected to the hopper 10, and the other side thereof is connected to the first feed inlet 111 through the pipeline 400. The second propulsion screw 11 is arranged inside the solid material pipeline 12, and the servo motor 13 is electrically connected to the controller 200 to drive the second propulsion screw 11 to push the solid phase material and convey the solid phase material into the processing pipeline 101. The second feeding unit 2 includes at least one second batching tank 20 for holding the aqueous phase material and a second metering pump 21. The second batching tank 20 is connected to the second feed inlet 112 through the pipeline 400, and the second metering pump 21 is arranged on the pipeline 400 to control a flow rate of the aqueous phase material entering the processing pipeline 101. The third feeding unit 3 includes at least one third batching tank 30 for holding the aqueous phase functional material and a third metering pump 31. The third batching tank 30 is connected to the third feed inlet 113 through the pipeline 400, and the third metering pump 31 is arranged on the pipeline 400 to control a flow rate of the aqueous phase functional material entering the processing pipeline 101. The fourth feeding unit 4 includes at least one fourth batching tank 40 for holding the oil phase functional material and a fourth metering pump 41. The fourth batching tank 40 is connected to the fourth feed inlet 114 through the pipeline 400, and the fourth metering pump 41 is arranged on the pipeline 400 to control a flow rate of the oil phase functional material entering the processing pipeline 101. The fifth feeding unit 5 includes at least one fifth batching tank 50 for holding the other ingredients and a fifth metering pump 51. The fifth batching tank 50 is connected to the fifth feed inlet 115 in the processing pipeline 101 through the pipeline 400, and the fifth metering pump 51 is arranged on the pipeline 400 to control a flow rate of the other ingredients entering the processing pipeline 101. A stirring apparatus 6 is arranged inside the second batching tank 20, the third batching tank 30, the fourth batching tank 40, and the fifth batching tank 50, respectively. The stirring apparatus 6 includes a stirring motor 60 electrically connected to the controller 200 and a stirring rod 61 connected to the stirring motor 60. The stirring motor 60 drives the stirring rod 61 to stir different materials in the batching tanks and preliminarily mix the materials evenly. In addition, the second batching tank 20, the third batching tank 30, the fourth batching tank 40, and the fifth batching tank 50 all have heating functions. Outer sides of the second batching tank 20, the third batching tank 30, the fourth batching tank 40, and the fifth batching tank 50 are provided with a tank sleeve 7, respectively. Each tank sleeve 7 is provided with a third temperature sensor 70, and the third temperature sensor 70 is electrically connected to the controller 200 to monitor the temperature of each batching tank. A pipe sleeve 401 is arranged at an outer side of the pipeline 400, a thermal insulation chamber 402 is formed between the pipe sleeve 401 and the pipeline 400, a hot water tank 403 and a hot water pump 404 are arranged at an outer side of the pipe sleeve 401, and the hot water tank 403, the hot water pump 404, and the thermal insulation chamber 402 are in communication with each other. The hot water tank 403 has a self-heating function, and the hot water pump 404 is connected to the controller 200 to drive hot water to circulate in the thermal insulation chamber 402 and the hot water tank 403, thus achieving the purpose of thermal insulation of the pipeline 400. The number of the hot water pumps 404 and the hot water tanks 403 can be independently set according to the temperature requirements of different pipelines 400. The man-machine interface 600 can display temperature values detected by the temperature sensors, pressure values detected by the pressure sensor 106, and rotational speeds of each motor, and can also set power of the hot water pumps and the rotational speeds of each motor. The discharging rate is digitally and automatically adjusted based on proportions of the materials in a formula, so that a hydrosol solution preparation procedure is simplified, data of the hydrosol solution preparation procedure is clearer, adjustment modes are more controllable, and time and labor costs are saved. As shown in FIG. 5, a preparation method for a hydrosol solution according to an embodiment of the present invention, including the following steps: step SI: classifying total materials required for hydrosol solution preparation according to material properties, and separately allocating classified materials to each of feeding stations 300 of a hydrosol solution preparation system for later use according to the material properties. The step SI specifically includes the following steps: step S10: classifying the total materials required for the hydrosol solution preparation into a solid phase material, an aqueous phase material, an aqueous phase functional material, an oil phase functional material, and other ingredients according to the material properties; step SI 1: simultaneously allocating the solid phase material to a first feeding unit 1, allocating the aqueous phase material to a second feeding unit 2, allocating the aqueous phase functional material to a third feeding unit 3, allocating the oil phase functional material to a fourth feeding unit 4, and allocating the other ingredients to a fifth feeding unit 5; and step S12: performing temperature control on each feeding unit according to the material properties of each material for later use. Step S2: switching on a heating system of the hydrosol solution preparation system to preheat a processing pipeline 101 of a mixing and shearing device 100, allowing temperature inside the processing pipeline 101 to meet processing requirements of the hydrosol solution. Specifically, an electromagnetic infrared heater 104 is switched on to preheat the processing pipeline 101 of the mixing and shearing device 100; whether the temperature inside the processing pipeline 101 meets the processing requirements of the hydrosol solution is determined in real time by a first temperature sensor 107; the processing pipeline 101 of the mixing and shearing device 100 is continuously heated by the electromagnetic infrared heater 104 if the first temperature sensor 107 detects that a temperature value is less than a preset minimum value; heating is stopped if the first temperature sensor 107 detects that the temperature value is greater than a preset maximum value; and the temperature inside the processing pipeline 101 is controlled to be within a temperature range required for processing of the hydrosol solution. Step S3: calculating and configuring a flow rate of the materials with each material property entering the processing pipeline 101. The step S3 specifically includes the following steps: step S30: calculating the flow rate of the materials with each material property entering the processing pipeline 101; specifically, a discharging flow rate of the discharge port 110 of the processing pipeline 101 being defined as Knit, where a range of K>ut is 50-300 kg / h; the flow rate of each material entering the processing pipeline 101 meeting the following conditions: Fa-P outxa; J b=l out b; Fc=Foutxc; Fd=Foutxd; and Fe=Foutxe; where Fa, Kb, Kc, Ka, and Fe are the flow rates of the solid phase material, the aqueous phase material, the aqueous phase functional material, the oil phase functional material, and the other ingredients entering the processing pipeline 101, respectively; and a, b, c, d, and e are mass proportions of the solid phase material, the aqueous phase material, the aqueous phase functional material, the oil phase functional material, and the other ingredients in the total materials, respectively. Step S31: allocating a calculated flow rate value of the materials with each material property to each of the feeding stations 300. By controlling the flow rate of each material, the proportion of each material required for the hydrosol solution can be controlled. Compared to a conventional method for controlling proportions of materials by manual weighing, this method is more efficient. Step S4: starting the mixing and shearing device 100 of the hydrosol solution preparation system, synchronously opening each of the feeding stations 300, conveying each material into the processing pipeline 101 according to a configured flow rate, and simultaneously mixing and shearing all the materials by a first screw 102 in the processing pipeline 101 to obtain a homogeneous hydrosol solution. The step S4 specifically includes the following steps: step S40: starting the mixing and shearing device 100 of the hydrosol solution preparation system, and synchronously opening each of the feeding stations 300; step S41: enabling the solid phase material and the aqueous phase material to enter the processing pipeline 101 from an upstream end 116 of the processing pipeline 101, and preliminarily shearing and mixing the solid phase material and the aqueous phase material under an action of the first screw 102 and then conveying to a downstream end 117 of the processing pipeline 101; step S42: enabling the aqueous phase functional material, the oil phase functional material, and the other ingredients to enter the processing pipeline 101 from the downstream end 117 of the processing pipeline 101, preliminarily mixing the aqueous phase functional material, the oil phase functional material, and the other ingredients with a mixture of the solid phase material and the aqueous phase material at the upstream end 116, and further conveying towards a discharge port 110; step S43: shearing and mixing the aqueous phase functional material, the oil phase functional material, and the other ingredients with the mixture of the solid phase material and the aqueous phase material again, and then discharging from the processing pipeline 101; step S44: discarding the solid phase material, the aqueous phase material, the aqueous phase functional material, the oil phase functional material, and the other ingredients that are not fully and evenly mixed in the processing pipeline 101 in an early working stage of the mixing and shearing device 100; and step S45: obtaining the homogeneous hydrosol solution at the discharge port 110 of the processing pipeline 101. Embodiment 1: A preparation method for a gummy candy (pectin) hydrosol solution, specifically including the following steps: step SI: classifying total materials required for preparation of a gummy candy hydrosol solution according to material properties, and separately allocating classified materials to each of feeding stations 300 of a hydrosol solution preparation system for later use according to the material properties. The step SI specifically includes the following steps: step S10: classifying the total materials required for the preparation of the gummy candy hydrosol solution into a solid phase material, an aqueous phase material, an aqueous phase functional material, an oil phase functional material, and other ingredients according to the material properties; the specific classification being shown in Table 1 below: Table 1 Classification table of total materials required for the gummy candy (pectin) hydrosol solution Name of mixture Proportion in the total materials (%) Name of material Proportion in the total materials (%) Solid phase material 36.486 White granulated sugar powder 34.171 Pectin 2.315 Aqueous phase material 54.283 Glucose syrup 35.935 Purified water 18.018 Sodium citrate 0.330 Oil phase functional material 0.417 Vitamin E oil 0.402 Acetate vitamin A oil 0.015 Aqueous phase functional material 6.831 Vitamin C 0.556 Vitamin D3 (powder) 0.056 Calcium pantothenate 0.590 Biotin 0.076 Sodium citrate 0.167 Glucose syrup 4.274 Purified water 1.112 Other ingredients 1.983 DL-malic acid 0.526 Anhydrous citric acid 0.240 Purified water 0.767 Peach essence 0.397 Black carrot concentrated juice 0.053 step Sil: simultaneously allocating the solid phase material to a first feeding unit 1, allocating the aqueous phase material to a second feeding unit 2, allocating the aqueous phase functional material to a third feeding unit 3, allocating the oil phase functional material to a fourth feeding unit 4, and allocating the other ingredients to a fifth feeding unit 5; and step S12: performing temperature control on each feeding unit according to the material properties of each material for later use. The temperature of various materials in the field of gummy candy processing belongs to the prior art and is not specifically limited herein. Suitable temperature will be determined based on processing requirements. Step S2: switching on a heating system of the hydrosol solution preparation system to preheat a processing pipeline 101 of a mixing and shearing device 100, allowing temperature inside the processing pipeline 101 to meet processing requirements of the hydrosol solution. Specifically, an electromagnetic infrared heater 104 is switched on to preheat the processing pipeline 101 of the mixing and shearing device 100; whether the temperature inside the processing pipeline 101 meets the processing requirements of the hydrosol solution is determined in real time by a first temperature sensor 107; the processing pipeline 101 of the mixing and shearing device 100 is continuously heated by the electromagnetic infrared heater 104 if the first temperature sensor 107 detects that a temperature value is less than a preset minimum value; heating is stopped if the first temperature sensor 107 detects that the temperature value is greater than a preset maximum value; and the temperature inside the processing pipeline 101 is controlled to be within a temperature range required for processing of the hydrosol solution. Step S3: calculating and configuring a flow rate of the materials with each material property entering the processing pipeline 101. The step S3 specifically includes the following steps: step S30: calculating the flow rate of the materials with each material property entering the processing pipeline 101; specifically, a discharging flow rate of the discharge port 110 of the processing pipeline 101 being defined as Tout, where Iout is 200 kg / h. The flow rates of various materials in the total materials required for the gummy candy (pectin) hydrosol solution entering the processing pipeline 101 meeting the following conditions as shown in Table 2 below: Table 2 Flow rates of various materials in the total materials required for the gummy candy (pectin) hydrosol solution Name of mixture Mass proportion in the total materials (%) Flow rate (kg / h) Meeting conditions Solid phase material 36.486 72.972 Va=200x36.486% Aqueous phase material 54.283 108.566 Vb=200x 54.283% Aqueous phase functional material 0.417 0.834 Vc=200><0.417% Oil phase functional material 6.831 13.662 Vd=200x6.831% Other ingredients 1.983 3.964 Ve=200xl.982% Step S31: allocating a calculated flow rate value of the materials with each material property to each of the feeding stations 300. Step S4: starting the mixing and shearing device 100 of the hydrosol solution preparation system, synchronously opening each of the feeding stations 300, conveying each material into the processing pipeline 101 according to a configured flow rate, and simultaneously mixing and shearing all the materials by a first screw 102 in the processing pipeline 101 to obtain a homogeneous hydrosol solution. The step S4 specifically includes the following steps: step S40: starting the mixing and shearing device 100 of the hydrosol solution preparation system, and synchronously opening each of the feeding stations 300; step S41: enabling the solid phase material and the aqueous phase material to enter the processing pipeline 101 from an upstream end 116 of the processing pipeline 101, and preliminarily shearing and mixing the solid phase material and the aqueous phase material under an action of the first screw 102 and then conveying to a downstream end 117 of the processing pipeline 101; step S42: enabling the aqueous phase functional material, the oil phase functional material, and the other ingredients to enter the processing pipeline 101 from the downstream end 117 of the processing pipeline 101, preliminarily mixing the aqueous phase functional material, the oil phase functional material, and the other ingredients with a mixture of the solid phase material and the aqueous phase material at the upstream end 116, and further conveying towards a discharge port 110; step S43: shearing and mixing the aqueous phase functional material, the oil phase functional material, and the other ingredients with the mixture of the solid phase material and the aqueous phase material again, and then discharging from the processing pipeline 101; step S44: discarding the solid phase material, the aqueous phase material, the aqueous phase functional material, the oil phase functional material, and the other ingredients that are not fully and evenly mixed in the processing pipeline 101 in an early working stage of the mixing and shearing device 100; and step S45: obtaining the homogeneous hydrosol solution at the discharge port 110 of the processing pipeline 101. Embodiment 2: A preparation method for a gummy candy (gelatin) hydrosol solution in this embodiment mainly differs from Embodiment 1 in that specific materials for each material property are different, and the flow rates of various materials entering the processing pipeline 101 are inconsistent, while the other procedures are consistent, which will not be repeated herein. The total materials required for the gummy candy (gelatin) hydrosol solution are classified according to the material properties as shown in Table 3 below: Table 3 Classification table of total materials required for the gummy candy (gelatin) hydrosol solution Name of mixture Proportion in the total materials (%) Name of material Proportion in the total materials (%) Solid phase material 36.530 220 Gelatin powder 9.480 White granulated sugar powder 27.050 Aqueous phase material 57.219 Glucose syrup 34.529 Purified water 22.690 Oil phase functional material 0.874 Lutein oil 0.552 Vitamin D oil 0.322 Aqueous phase functional material 2.034 Ferric pyrophosphate 0.500 Sodium citrate 0.143 Glucose syrup 1.143 Purified water 0.248 Other ingredients 3.343 Jujube essence 0.250 Vegetable carbon black 0.100 Citric acid 0.950 Glucose syrup 0.950 Purified water 1.093 A discharging flow rate of the discharge port 110 of the processing pipeline 101 is defined as Tout, where Tout is 200 kg / h. The flow rates of various materials in the total materials required for the gummy candy (gelatin) hydrosol solution entering the processing pipeline 101 meet the following conditions as shown in Table 4 below: Table 4 Flow rates of various materials in the total materials required for the gummy candy (gelatin) hydrosol solution Name of mixture Proportion in the total materials (%) Flow rate (kg / h) Meeting conditions Solid phase material 36.530 73.060 Va=200x36.530% Aqueous phase material 57.219 114.438 Vb=200x57.219% Aqueous phase functional material 0.874 1.748 Vc=200x0.874% Oil phase functional material 2.034 4.068 Vd=200x2.034% Other ingredients 3.343 6.686 Ve=200x3.343% Embodiment 3: A preparation method for a gummy candy (carrageenan) hydrosol solution in this embodiment mainly differs from Embodiment 1 in that specific materials for each material property are different, and the flow rates of various materials entering the processing pipeline 101 are inconsistent, while the other procedures are consistent, which will not be repeated herein. The total materials required for the gummy candy (carrageenan) hydrosol solution are classified according to the material properties as shown in Table 5 below: Table 5 Classification table of total materials required for the gummy candy (carrageenan) hydrosol solution Name of mixture Proportion in the total materials (%) Name of material Proportion in the total materials (%) Solid phase material 33.620 White granulated sugar powder 30.370 Carrageenan 3.250 Aqueous phase material 61.234 Glucose syrup 35.074 Sodium citrate 0.270 Purified water 25.890 Oil phase functional material 0.993 Vitamin E oil 0.463 Vitamin A oil 0.530 Aqueous phase functional material 1.153 Vitamin C 0.891 Vitamin B1 0.262 Other ingredients 3.000 Annatto 0.280 Sweet orange essence 0.300 Citric acid 0.930 Purified water 1.490 A discharging flow rate of the discharge port 110 of the processing pipeline 101 is defined as f out, where Tout is 200 kg / h. The flow rates of various materials in the total materials required for the gummy candy (carrageenan) hydrosol solution entering the processing pipeline 101 meet the following conditions as shown in Table 6 below: Table 6 Flow rates of various materials in the total materials required for the gummy candy (carrageenan) hydrosol solution Name of mixture Proportion in the total materials (%) Flow rate (kg / h) Meeting conditions Solid phase material 33.62 67.240 Va=200><33.62% Aqueous phase material 61.234 122.468 Vb=200x6 1.234% Aqueous phase functional material 0.993 1.986 Vc=200x0.993% Oil phase functional material 1.153 2.306 Vd=200x 1.153% Other ingredients 3.000 6.000 Ve=200x3.000% Embodiment 4: A preparation method for a soft capsule rubber hydrosol solution in this embodiment mainly differs from Embodiment 1 in that specific materials for each material property are different, and the flow rates of various materials entering the processing pipeline 101 are inconsistent, while the other procedures are consistent, which will not be repeated herein. The total materials required for the soft capsule rubber hydrosol solution are classified according to the material properties as shown in Table 7 below: Table 7 Classification table of total materials required for the soft capsule rubber hydrosol solution Name of mixture Proportion in the total materials (%) Name of material Proportion in the total materials (%) Solid phase material 45.0 Gelatin granules 45.0 Aqueous phase material 50.0 Glycerol 18.0 Pure water 32.0 Other ingredients 5.0 Caramel color 0.8 Water 4.2 A discharging flow rate of the discharge port 110 of the processing pipeline 101 is defined as Tout, where Com is 250 kg / h. The flow rates of various materials in the total materials required for the soft capsule rubber hydrosol solution entering the processing pipeline 101 meet the following conditions as shown in Table 8 below: Table 8 Flow rates of various materials in the total materials required for the soft capsule rubber hydrosol solution Name of mixture Proportion in the total materials (%) Flow rate (kg / h) Meeting conditions Solid phase material 45.0 112.5 Va=250x45.0% Aqueous phase material 50.0 125.0 Vb=250x50.0% Other 5.0 12.5 Ve=250x5.0% ingredients The present invention has the following beneficial effects: 1. The system and preparation method can be applied to the preparation procedure of hydrosol solutions in daily chemicals, food, and drugs, and can simultaneously introduce various functional components and auxiliary materials online. Especially, they have more advantages in the preparation of relatively viscous water-soluble systems such as gel jelly solutions, soft capsule rubber solutions, and gummy candy syrup. 2. The process and system also have unique advantages in the aspect of thermosensitive functional materials. The first feeding unit for storing the solid phase material and the second feeding unit for storing the aqueous phase material are connected to one side of the processing pipeline close to the drive motor, and after the materials entering an online material mixing and shearing device are fully dispersed, dissolved, and sheared, the third feeding unit and the fourth feeding unit for storing the functional materials and the fifth feeding unit for storing the other ingredients are connected near an outlet end of the processing pipeline. Therefore, the time for heating, mixing, and shearing of the functional materials is reduced, the stability of the functional components is greatly improved, the loss of nutrients is reduced, and higher functional content and better quality of the obtained hydrosol solution are achieved. 3. Compared to a conventional hydrosol solution preparation process, this process changes the procedure of gradually feeding, mixing, and boiling, adopts a material mixing and shearing device and a quantitative feeding system to cascade the hydrosol solution preparation procedure, and digitally and automatically adjusts a discharging rate based on proportions of the materials in a formula. Therefore, the hydrosol solution preparation procedure is simplified, data of the hydrosol solution preparation procedure is clearer, adjustment modes are more controllable, and time and labor costs are saved. Compared to batch production, this process can achieve continuous production of the hydrosol solution during preparation, thereby further reducing production costs and improving labor efficiency. 4. The system and process require a short time for hydrosol solution preparation, and only take the time to pass through the online material mixing and shearing device from the feeding of each material to the final hydrosol solution preparation. Therefore, the time consumed by the whole procedure is reduced, and the total time for the hydrosol solution preparation does not exceed 3 min, which greatly improves the production efficiency. 5. The working intensity of operators is reduced, a simple manufacturing procedure and high continuity are achieved, the occupation of factory space is reduced, and the economic benefits are improved. The foregoing embodiments only express a plurality of implementations of the present invention, and the description was relatively specific and detailed, but it should not be understood as a limitation to the patent scope of the present invention. It should be noted that for those of ordinary skill in the art, several modifications and improvements can be made without departing from the concept of the present invention and these modifications and improvements should all fall within the protection scope of the present invention. Therefore, the protection scope of the present invention patent shall be subject to the appended claims.

Claims

1. A preparation method for a hydrosol solution, comprising the following steps:classifying total materials required for hydrosol solution preparation according to material properties, and separately allocating classified materials to each of feeding stations (300) of a hydrosol solution preparation system for later use according to the material properties;switching on a heating system of the hydrosol solution preparation system to preheat a processing pipeline (101) of a mixing and shearing device (100), allowing temperature inside the processing pipeline (101) to meet processing requirements of the hydrosol solution;calculating and configuring a flow rate of the materials with each material property entering the processing pipeline (101); andstarting the mixing and shearing device (100) of the hydrosol solution preparation system, synchronously opening each of the feeding stations (300), conveying each material into the processing pipeline (101) according to a configured flow rate, and simultaneously mixing and shearing all the materials by a first screw (102) in the processing pipeline (101) to obtain a homogeneous hydrosol solution.

2. The preparation method for a hydrosol solution according to claim 1, wherein the step of classifying total materials required for hydrosol solution preparation according to material properties, and separately allocating classified materials to each of feeding stations (300) of the hydrosol solution preparation system for later use according to the material properties comprises the following steps:classifying the total materials required for the hydrosol solution preparation into a solid phase material, an aqueous phase material, an aqueous phase functional material, an oil phase functional material, and other ingredients according to the material properties;simultaneously allocating the solid phase material to a first feeding unit (1), allocating the aqueous phase material to a second feeding unit (2), allocating the aqueous phase functional material to a third feeding unit (3), allocating the oil phase functional material to a fourth feeding unit (4), and allocating the other ingredients to a fifth feeding unit (5); andperforming temperature control on each feeding unit according to the material properties of each material for later use.

3. The preparation method for a hydrosol solution according to claim 2, wherein the step of starting the mixing and shearing device (100) of the hydrosol solution preparation system, synchronously opening each of the feeding stations (300), conveying each material into the processing pipeline (101) according to the configured flow rate, and simultaneously mixing andshearing all the materials by the first screw (102) in the processing pipeline (101) to obtain the homogeneous hydrosol solution specifically comprises the following steps:starting the mixing and shearing device (100) of the hydrosol solution preparation system, and synchronously opening each of the feeding stations (300);enabling the solid phase material and the aqueous phase material to enter the processing pipeline (101) from an upstream end (116) of the processing pipeline (101), and preliminarily shearing and mixing the solid phase material and the aqueous phase material under an action of the first screw (102) and then conveying to a downstream end (117) of the processing pipeline (101);enabling the aqueous phase functional material, the oil phase functional material, and the other ingredients to enter the processing pipeline (101) from the downstream end (117) of the processing pipeline (101), preliminarily mixing the aqueous phase functional material, the oil phase functional material, and the other ingredients with a mixture of the solid phase material and the aqueous phase material at the upstream end (116), and further conveying towards a discharge port (110);shearing and mixing the aqueous phase functional material, the oil phase functional material, and the other ingredients with the mixture of the solid phase material and the aqueous phase material again, and then discharging from the processing pipeline (101); andobtaining the homogeneous hydrosol solution at the discharge port (110) of the processing pipeline (101).

4. The preparation method for a hydrosol solution according to claim 2, wherein the step of starting the mixing and shearing device (100) of the hydrosol solution preparation system, synchronously opening each of the feeding stations (300), conveying each material into the processing pipeline (101) according to a configured flow rate, and simultaneously mixing and shearing all the materials by the first screw (102) in the processing pipeline (101) to obtain the homogeneous hydrosol solution further comprises the following steps:discarding the solid phase material, the aqueous phase material, the aqueous phase functional material, the oil phase functional material, and the other ingredients that are not fully and evenly mixed in the processing pipeline (101) in an early working stage of the mixing and shearing device (100).

5. The preparation method for a hydrosol solution according to claim 2, wherein the step of calculating and configuring the flow rate of the materials with each material property entering the processing pipeline (101) comprises:calculating the flow rate of the materials with each material property entering the processingpipeline (101); andallocating a calculated flow rate value of the materials with each material property to each of the feeding stations (300).

6. The preparation method for a hydrosol solution according to claim 5, wherein the step of calculating the flow rate of the materials with each material property entering the processing pipeline (101) comprises:defining a discharging flow rate of the discharge port (110) of the processing pipeline (101) as Fout, wherein a range of Fout is 50-300 kg / h;the flow rate of each material entering the processing pipeline (101) meeting the following conditions:FH.mXa;Fb Foutxb,Fc Foutxc,Fd=Foutxd; andFe=Foutxe; whereinFa, Fb, Fc, Fa, and Fe are the flow rates of the solid phase material, the aqueous phase material, the aqueous phase functional material, the oil phase functional material, and the other ingredients entering the processing pipeline (101), respectively; and a, b, c, d, and e are mass proportions of the solid phase material, the aqueous phase material, the aqueous phase functional material, the oil phase functional material, and the other ingredients in the total materials, respectively.

7. The preparation method for a hydrosol solution according to claim 1, wherein the step of switching on the heating system of the hydrosol solution preparation system to preheat the processing pipeline (101) of the mixing and shearing device (100), allowing temperature inside the processing pipeline (101) to meet processing requirements of the hydrosol solution comprises:switching on an electromagnetic infrared heater (104) to preheat the processing pipeline (101) of the mixing and shearing device (100);determining whether the temperature inside the processing pipeline (101) meets the processing requirements of the hydrosol solution in real time by a first temperature sensor (107);continuously heating the processing pipeline (101) of the mixing and shearing device (100) by the electromagnetic infrared heater (104) if the first temperature sensor (107) detects that a temperature value is less than a preset minimum value;stopping heating if the first temperature sensor (107) detects that the temperature value is greater than a preset maximum value; andcontrolling the temperature inside the processing pipeline (101) to be within a temperature range required for processing of the hydrosol solution.

8. A preparation system based on the preparation method for a hydrosol solution according to any one of claims 1 to 7, comprising:a mixing and shearing device (100);a controller (200); anda plurality of feeding stations (300), configured to store materials with different material properties, respectively; whereinthe plurality of feeding stations (300) are all connected to the mixing and shearing device (100) to convey the materials with different material properties into the mixing and shearing device (100), the controller (200) is electrically connected to the plurality of feeding stations (300) to control material conveying rates of the plurality of feeding stations (300), respectively, and the controller (200) is electrically connected to the mixing and shearing device (100) to control the mixing and shearing device (100) to mix and shear the materials with different material properties.

9. The preparation system for a hydrosol solution according to claim 8, wherein the mixing and shearing device (100) comprises a processing pipeline (101), a first screw (102), and a drive motor (103), the feeding stations (300) are in communication with the processing pipeline (101) to convey the materials with different material properties into the processing pipeline (101), the first screw (102) is arranged inside the processing pipeline (101), the drive motor (103) is electrically connected to the controller (200) to drive the first screw (102) to mix and shear the materials in the processing pipeline (101) so as to obtain the hydrosol solution, and the first screw (102) discharges an obtained hydrosol solution from a discharge port (110) of the processing pipeline (101).

10. The preparation system for a hydrosol solution according to claim 9, wherein the plurality of feeding stations (300) comprise a first feeding unit (1) for storing a solid phase material, a second feeding unit (2) for storing an aqueous phase material, a third feeding unit (3) for storing an aqueous phase functional material, a fourth feeding unit (4) for storing an oil phase functional material, and a fifth feeding unit (5) for storing other ingredients, and the first feeding unit (1), the second feeding unit (2), the third feeding unit (3), the fourth feeding unit (4), and the fifth feeding unit (5) are all in communication with the processing pipeline (101) through a pipeline (400).

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