CN219984521U

CN219984521U - Preparation system of hydrosol liquid

Info

Publication number: CN219984521U
Application number: CN202321028730.3U
Authority: CN
Inventors: 张国栋; 陈中科; 夏旭东; 束磊; 朱晴; 朱冰清; 黄惠
Original assignee: Jiangsu Aiju Health Technology Co ltd
Current assignee: Jiangsu Aiju Health Technology Co ltd
Priority date: 2023-04-28
Filing date: 2023-04-28
Publication date: 2023-11-10
Anticipated expiration: 2033-04-28

Abstract

The utility model discloses a preparation system of hydrosol liquid, which comprises a mixing and shearing device, a controller and a plurality of feeding stations, wherein the plurality of feeding stations are respectively used for storing materials with different material properties, the plurality of feeding stations are connected with the mixing and shearing device and are used for conveying the materials with different material properties into the mixing and shearing device, the controller is electrically connected with the plurality of feeding stations and is respectively used for controlling the speed of conveying the materials by the plurality of feeding stations, the controller is electrically connected with the mixing and shearing device and is used for controlling the operation of the mixing and shearing device, and the mixing and shearing device is used for simultaneously mixing and shearing the materials with different material properties to obtain a water gel solution. The utility model can reduce the working strength of operators, has simple manufacturing process and high continuity, and reduces the time consumed by the whole working procedure.

Description

Preparation system of hydrosol liquid

Technical Field

The utility model relates to the technical field of hydrosol processing, in particular to a hydrosol preparation system.

Background

Water-soluble colloid is a high-molecular material with strong hydrophilicity, and can be dissolved or swelled in water to form a relatively viscous aqueous solution or dispersion system, and the aqueous solution or dispersion system is commonly called a high-molecular aqueous solution or a water-soluble colloid solution. Hydrophilic groups in the water-soluble colloid not only enable the water-soluble colloid to have water solubility, but also have chemical functions and various physical functions such as dispersion, flocculation, tackifying, drag reduction, adhesion, film formation, gel formation, chelation and the like, so that the water-soluble colloid has wide application in daily chemicals, food and pharmaceutical industries.

Because of the complexity of the structure of the high molecular weight and the polydispersity, the dissolution phenomenon is much more complex than that of small molecular substances. The sizes of the polymer and the solvent molecules are greatly different, the molecular movement speeds of the polymer and the solvent molecules are also greatly different, the solvent molecules can permeate into the polymer relatively quickly, and the diffusion of the polymer into the solvent is very slow. Thus, the dissolution process of the polymer is performed in two stages, namely, solvent molecules penetrate into the polymer to expand the volume of the polymer, which is called "swelling", and then the polymer is uniformly dispersed in the solvent to form a completely dissolved molecular dispersion homogeneous system. The whole dissolution process requires a long time, and generally requires conditions such as stirring, shearing and homogenization. Meanwhile, in order to accelerate the dissolution of certain polymer colloids, the dissolution needs to be carried out under a higher temperature condition.

The water-soluble colloid is widely applied in food, is an indispensable food ingredient part in some food varieties, and plays an important role. For example, in the food industry, products such as jelly products, soft sweets, soft capsules, etc. all require the application of water-soluble gums and the preparation of water-soluble solutions to obtain the final products.

The existing hydrosol preparation process, such as the hydrosol preparation process of gel soft sweets, comprises the following steps of: adding white granulated sugar, glucose syrup and water into a sugar dissolving tank for dilution; sol: conveying the diluted solution into a colloid tank, and adding vegetable gum and a large amount of water to carry out high-temperature sol; sugar boiling: after the sol is passed, the sol is transferred into a sugar boiling tank for boiling, and the water in the sol is filtered to obtain syrup; temporary storage: conveying the syrup to a temporary storage tank for temporary storage; sugar solution preparation: and conveying the sugar solution in the temporary storage tank to an effect mixing tank, and adding the required effect components to obtain the required water-soluble glue solution of the gel soft sweet.

The hydrosol solution process is carried out by a mode of dissolving sugar, dissolving the sol, decocting the sugar and stirring and mixing the efficacy, the preparation process is carried out by multiple persons according to the preparation process, the working strength of operators is high, the preparation process is complex, the continuity is poor, the whole preparation process takes 4-5 hours, the whole process consumes long time, and the production cost is high.

Disclosure of Invention

Aiming at the defects of the prior art, the utility model provides a system for preparing a water-soluble glue solution, which can reduce the working strength of operators, has simple manufacturing process and high continuity and reduces the time consumed by the whole process.

The utility model is realized by the following technical scheme:

the utility model provides a preparation system of hydrosol liquid, includes thoughtlessly cuts equipment, controller and a plurality of feed station, and a plurality of feed stations are used for depositing the material of different material properties respectively, and a plurality of feed stations all are connected with thoughtlessly cut equipment and with the material of different material properties is carried in the thoughtlessly cut equipment, the controller is connected with a plurality of feed stations electricity and is controlled the speed that a plurality of feed stations carried the material respectively, the controller with it connects and controls to thoughtlessly cut equipment electricity thoughtlessly cut the operation of equipment, thoughtlessly cut equipment and be used for mixing simultaneously and cut the material of different material properties in order to obtain the hydrocolloid solution.

Further, the mixing and shearing equipment comprises a processing pipeline, a first screw and a driving motor, wherein the feeding station is communicated with the processing pipeline and used for conveying materials with different material properties into the processing pipeline, the first screw is arranged in the processing pipeline, the driving motor is electrically connected with the controller and used for driving the first screw to mix and shear all materials in the processing pipeline simultaneously to obtain hydrosol liquid, and the first screw discharges the obtained hydrosol liquid from a discharge port of the processing pipeline.

Further, the plurality of feeding stations comprise a first feeding unit for storing solid-phase materials and a second feeding unit for storing water-phase materials, and the first feeding unit and the second feeding unit are communicated with the processing pipeline through pipelines.

Further, the plurality of feeding stations further comprise a third feeding unit for storing water-phase functional materials and a fourth feeding unit for storing oil-phase functional materials, and the third feeding unit and the fourth feeding unit are communicated with the processing pipeline through pipelines.

Further, one end of the processing pipeline, which is close to the driving motor, is provided with a first feeding port and a second feeding port, one end of the processing pipeline, which is close to the discharge port, is provided with a third feeding port and a fourth feeding port, the first feeding unit is connected with the first feeding port, the second feeding unit is connected with the second feeding port, the third feeding unit is connected with the third feeding port, and the fourth feeding unit is connected with the fourth feeding port.

Further, the first feeding unit comprises a hopper for storing solid-phase materials, a second pushing screw, a solid-phase material pipeline and a servo motor, one side of the solid-phase material pipeline is connected with the hopper, the other side of the solid-phase material pipeline is connected with the first feeding port through a pipeline, the second pushing screw is arranged in the solid-phase material pipeline, and the servo motor is electrically connected with the controller and used for driving the second pushing screw to mix and shear the solid-phase materials and send the solid-phase materials into the processing pipeline.

Further, the second feeding unit comprises at least one second batching tank for placing water phase materials and a second metering pump, the second batching tank is connected with the second feeding port through a pipeline, and the second metering pump is arranged on the pipeline and used for controlling the flow rate of the water phase materials entering the processing pipeline.

Further, the third feeding unit comprises at least one third batching tank for placing the water-phase functional materials and a third metering pump, the third batching tank is connected with the third feeding port through a pipeline, and the third metering pump is arranged on the pipeline and used for controlling the flow rate of the water-phase functional materials entering the processing pipeline.

Further, the fourth feeding unit comprises at least one fourth batching tank for placing oil phase efficacy materials and a fourth metering pump, the fourth batching tank is connected with the fourth feeding port through a pipeline, and the fourth metering pump is arranged on the pipeline and used for controlling the flow rate of the oil phase efficacy materials entering the processing pipeline.

Further, the first screw comprises a plurality of groups of pushing sections and shearing sections, and the pushing sections and the shearing sections are arranged at intervals.

Further, the first feed port, the second feed port, the third feed port and the fourth feed port correspond to the positions of the pushing sections in the processing pipeline.

Further, the first feed inlet and the second feed inlet correspond to the same section of the pushing section in the processing pipeline, and the third feed inlet and the fourth feed inlet correspond to the same section of the pushing section in the processing pipeline.

Further, at least one group of shearing sections is arranged on the part of the first screw rod located between the second feeding hole and the third feeding hole.

Further, at least one group of the shearing sections is arranged on the part of the first screw rod located between the third feed inlet and the discharge outlet.

Further, the propelling section is formed by combining a plurality of groups of propelling thread modules, the shearing section is formed by combining a plurality of groups of shearing thread modules, the pitch d1 of the propelling thread modules of the propelling section is 36-112mm, and the pitch d2 of the shearing thread modules of the shearing section is 22-96mm.

Further, the plurality of feeding stations further comprise a fifth feeding unit for storing other ingredients, the fifth feeding unit comprises at least one fifth ingredient tank for storing other ingredients and a fifth metering pump, the fifth ingredient tank is connected with a fifth feeding port on the processing pipeline through a pipeline, the fifth feeding port and the third feeding port correspond to the same section of the pushing section in the processing pipeline, and the fifth metering pump is arranged on the pipeline and used for controlling the flow rate of the other ingredients entering the processing pipeline.

Compared with the prior art, the utility model has the advantages that:

1. the system and the preparation method can be applied to the preparation process of water-soluble glue liquid in daily chemicals, foods and medicines, and simultaneously can synchronously introduce various functional components and auxiliary material parts on line, and particularly have more advantages in a relatively viscous water-soluble system, such as the preparation of gel jelly glue liquid, soft capsule glue skin glue liquid, soft candy glue liquid and the like.

2. The process and the system have unique advantages in the direction of thermosensitive effect materials, the first feeding unit for storing solid-phase materials and the second feeding unit for storing water-phase materials are connected to one side of the processing pipeline close to the driving motor, so that after materials entering the on-line material mixing and shearing equipment are fully dispersed, dissolved and sheared, the third feeding unit and the fourth feeding unit for storing the effect materials and the fifth feeding unit for storing other ingredients are connected to the outlet end of the processing pipeline, the heating, mixing and shearing time of the effect materials is reduced, the stability of the effect components is greatly improved, the loss of nutrient substances is reduced, the effect content of the obtained hydrosol is higher, and the quality is better.

3. Compared with the traditional glue solution preparation process, the process changes the gradual feeding, mixing and boiling processes, adopts the glue solution preparation process of series connection of material mixing and shearing equipment and a quantitative feeding system, adopts a digital automatic mode to adjust the discharging rate according to the proportion of materials in the formula, simplifies the glue solution preparation process, ensures that the data of the glue solution preparation process is clearer, the adjustment mode is more controllable, and saves the time and labor cost; compared with batch production, the process can realize continuous production of glue solution preparation, can reduce production cost and improve labor efficiency.

4. The system and the process have the advantages that the time for preparing the hydrosol is short, the time for entering the final glue solution from each material to prepare the final glue solution only needs to pass through on-line material mixing and shearing equipment, the time consumed by the whole process is reduced, the preparation time of the whole hydrosol is not more than 3 mm, and the production efficiency is greatly improved.

5. The working strength of operators is reduced, the manufacturing process is simple, the continuity is high, the occupied space of a factory building is reduced, and the economic benefit is improved.

Drawings

FIG. 1 is a schematic diagram of a system for preparing a hydrosol according to an embodiment of the present utility model;

FIG. 2 is a schematic diagram of a thermal insulation pipeline structure;

FIG. 3 is a schematic view of the structure of the first screw;

FIG. 4 is a control block diagram of a system for preparing a water-soluble solution;

FIG. 5 is a flow chart of a method for preparing a water-soluble glue solution.

100. A shearing mixing device; 101. processing a pipeline; 110. a discharge port; 111. a first feed port; 112. a second feed inlet; 113. a third feed inlet; 114. a fourth feed inlet; 115. a fifth feed inlet; 102. a first screw; 121. a propulsion section; 122. a shearing section; 123. advancing the thread module; 124. shearing a thread module; 103. a driving motor; 104. an electromagnetic infrared heater; 105. a thermal insulation sleeve; 106. a pressure sensor; 107. a first temperature sensor; 108. a second temperature sensor; 109. a frequency converter; 200. a controller; 300. a feed station; 1. a first feeding unit; 10. a hopper; 11. a second pusher screw; 12. a solid material conduit; 13. a servo motor; 2. a second feeding unit; 20. a second compounding tank; 21. a second metering pump; 3. a third feeding unit; 30. a third compounding tank; 31. a third metering pump; 4. a fourth feeding unit; 40. a fourth batching tank; 41. a fourth metering pump; 5. a fifth feeding unit; 50. a fifth batching tank; 51. a fifth metering pump; 6. a stirring device; 60. a stirring motor; 61. a stirring rod; 7. a tank sleeve; 70. a third temperature sensor; 400. a pipeline; 401. a pipe sleeve; 402. a heat preservation cavity; 403. a hot water tank; 404. a hot water pump; 500. a bottom plate; 501. a base; 502. a mounting plate; 503. a first support frame; 504. a second support frame; 505. a support plate; 600. and a human-computer interface.

Detailed Description

The technical scheme of the utility model is further described in non-limiting detail below with reference to the preferred embodiments and the accompanying drawings. In the description of the present utility model, it is to be understood that the terms "center", "longitudinal", "transverse", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", "axial", "radial", "circumferential", etc. refer to the azimuth or positional relationship based on the azimuth or positional relationship shown in the drawings. Furthermore, the terms "first," "second," and the like, are used for descriptive purposes only and are not to be construed as indicating or implying a relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defining "a first" or "a second" may explicitly or implicitly include at least one such feature. In the description of the present utility model, the meaning of "plurality" means at least two, for example, two, three, etc., unless specifically defined otherwise. The embodiments described below by referring to the drawings are illustrative and intended to explain the present utility model and should not be construed as limiting the utility model.

As shown in fig. 1 to 4, a preparation system of an hydrosol solution according to an embodiment of the present utility model includes a mixing and shearing apparatus 100, a controller 200, a plurality of feeding stations 300 and a man-machine interface 600, wherein the feeding stations 300 are connected to the mixing and shearing apparatus 100 through a pipeline 400 and convey materials with different material properties to the mixing and shearing apparatus 100, the controller 200 is electrically connected to the plurality of feeding stations 300 and controls the speed of conveying the materials by each feeding station 300, the controller 200 is electrically connected to the mixing and shearing apparatus 100 and controls the operation of the mixing and shearing apparatus 100, the mixing and shearing apparatus 100 is used for simultaneously mixing and shearing the materials with different material properties to obtain the hydrosol solution, and after the processing is completed, the materials with different material properties are discharged from the mixing and shearing apparatus 100, and the man-machine interface 600 and the controller 200 are electrically connected to send working instructions and display various parameters of the system.

The shearing mixing device 100 comprises a processing pipeline 101, a first screw rod 102, a driving motor 103 and an electromagnetic infrared heater 104, wherein a feeding station 300 is communicated with the processing pipeline 101 and used for conveying materials with different material properties into the processing pipeline 101, the electromagnetic infrared heater 104 is arranged outside the processing pipeline 101 and is electrically connected with a controller 200, a heat insulation sleeve 105 is arranged outside the electromagnetic infrared heater 104, the first screw rod 102 is arranged in the processing pipeline 101, the driving motor 103 is fixedly connected with the first screw rod 102, the driving motor 103 is electrically connected with the controller 200 and used for driving the first screw rod 102 to mix and shear all the materials in the processing pipeline 101 simultaneously to obtain hydrosol, and the first screw rod 102 discharges the obtained hydrosol from a discharge outlet 110 of the processing pipeline 101.

The shearing apparatus 100 further includes a base plate 500, and the processing pipe 101 and the driving motor 103 are fixedly disposed on the base plate 500.

The bottom plate 500 includes a base 501, a mounting plate 502 fixed on the base 501, and a first supporting frame 503, the processing pipeline 101 is fixed above the first supporting frame 503, the driving motor 103 is fixed on the mounting plate 502, and a motor shaft (not shown) of the driving motor 103 passes through the first supporting frame 503 to drive the first screw 102 to rotate.

The mounting plate 502 is also fixed with a second supporting frame 504 and a supporting plate 505, the second supporting frame 504 is fixedly connected with the solid material pipeline 12, and the supporting plate 505 is fixedly connected with the motor 13. The second feeding unit 2, the third feeding unit 3, the fourth feeding unit 4 and the fifth feeding unit 5 are all fixed above the processing pipe 101 by means of a mounting bracket (not shown).

Specifically, the controller 200 controls the driving motor 103 to operate through the inverter 109.

The pressure sensor 106 is arranged at the discharge outlet 110, the pressure sensor 106 is electrically connected with the controller 200, when the pressure sensor 106 detects that the pressure value at the discharge outlet 110 is higher than the set threshold value, a signal is fed back to the controller 200, and the controller 200 controls the driving motor 103 to reduce the rotating speed, otherwise, the rotating speed of the driving motor 103 is increased.

The processing pipeline 101 is internally provided with a first temperature sensor 107 for monitoring the temperature of materials in the processing pipeline 101, the heat preservation sleeve 105 is internally provided with a second temperature sensor 108, the first temperature sensor 107 and the second temperature sensor 108 are both connected with the controller 200, when the first temperature sensor 107/the second temperature sensor 108 are lower 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 the temperature in the processing pipeline 101 to be controlled in a temperature range required by processing of the hydrosol. In addition, the electromagnetic infrared heater 104 may be controlled by the controller 200 to continuously heat the processing pipe 101, and the first temperature sensor 107 and the second temperature sensor 108 may be used to monitor whether the temperatures in the processing pipe 101 and the thermal insulation sleeve 105 meet the operation requirements.

The processing pipeline 101 is provided with a plurality of feeding holes, the number of the feeding holes is consistent with that of the feeding stations 300, and each feeding station 300 is connected with one of the feeding holes. In this embodiment, five feed inlets are provided, 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, respectively, wherein the first feed inlet 111 and the second feed inlet 112 are adjacently disposed at one end of the processing pipeline 101 close to the driving motor 103, and the third feed inlet 113, the fourth feed inlet 114 and the fifth feed inlet 115 are adjacently disposed at one end of the processing pipeline 101 close to the discharge outlet 110 (i.e., one end of the processing pipeline 101 far away from the driving motor 103. Because the ratio of solid phase materials and aqueous phase materials in the materials required by the aqueous solution is relatively large, the first feed inlet 111 and the second feed inlet 112 corresponding to the first feed inlet 1 and the second feed inlet 2 corresponding to the second feed inlet for storing the solid phase materials are adjacently disposed at one end of the processing pipeline 101 close to the driving motor 103, respectively, so as to enable the solid phase materials and the aqueous phase materials to have enough time in the processing pipeline 101, to achieve sufficient shearing, and then achieve the effects of shearing with small proportion of the aqueous phase materials, and other materials, and the necessary energy consumption of the materials are not designed reasonably.

In this embodiment, a twin-screw shearing device is adopted, two completely identical first screws 102 are matched to cooperate to mix and shear materials in the processing pipeline 101, the diameter of each first screw 102 is 75mm, each first screw 102 comprises a plurality of groups of pushing sections 121 and shearing sections 122, the pushing sections 121 and the shearing sections 122 are arranged at intervals, the pushing sections 121 are formed by combining a plurality of groups of pushing thread modules 123, and the shearing sections 122 are formed by combining a plurality of groups of shearing thread modules 124. The first feed port 111, the second feed port 112, the third feed port 113, the fourth feed port 114 and the fifth feed port 115 correspond to the positions of the pushing sections 121 in the processing pipeline 101, and the first feed port 111 and the second feed port 112 correspond to the same pushing sections 121 in the processing pipeline 101, the third feed port 113, the fourth feed port 114 and the fifth feed port 115 correspond to the same pushing sections 121 in the processing pipeline 101, further, the part of the first screw 102 between the second feed port 112 (the first feed port 111) and the third feed port 113 (the fourth feed port 114/the fifth feed port 115) is provided with at least one set of shearing sections 122, and the part of the first screw 102 between the third feed port 113 (the fourth feed port 114/the fifth feed port 115) and the discharge port 110 is provided with at least one set of shearing sections 122, i.e. the materials entering from each feed port are first mixed by the pushing sections 121 and pushed into the shearing sections 122, and then mixed with the shearing sections 122 sufficiently. The first screw rod is mutually spaced through advancing section 121 and shearing section 122, advances section 121 can be very fast with different kinds of materials mixture, through shearing section 122 to its shearing, advance the screw pitch of the screw thread module 123 of advancing of section 121 big, promotes the distance that the material marched in the unit time length, has improved the machining efficiency to the material.

Wherein the pitch d1 of the push thread module 123 of the push section 121 is 36-112mm, and the pitch d2 of the shear thread module 124 of the shear section 122 is 22-96mm. In this embodiment, the pitch d1 of the push thread module 123 of the push section 121 is specifically 72mm, the total length of the push section 121 is 216mm, the pitch d2 of the shear thread module 124 of the shear section 122 is specifically 56mm, and the total length of the shear section is 168mm.

In this embodiment, the controller 200 selects the PLC S7-1200.

The feeding station 300 comprises a first feeding unit 1 for storing solid phase materials, a second feeding unit 2 for storing aqueous phase materials, a third feeding unit 3 for storing aqueous phase functional materials, a fourth feeding unit 4 for storing oil phase functional materials, and a fifth feeding unit 5 for storing 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 communicated with the processing pipeline 101 through a pipeline 400. Specifically, the first feeding unit 1 is connected to a first feeding port 111 on the processing pipeline 101, the second feeding unit 2 is connected to a second feeding port 112 on the processing pipeline 101, the third feeding unit 3 is connected to a third feeding port 113 on the processing pipeline 101, the fourth feeding unit 4 is connected to a fourth feeding port 114 on the processing pipeline 101, and the fifth feeding unit 5 is connected to a fifth feeding port 115 on the processing pipeline 101.

The first feeding unit 1 comprises a hopper 10 for storing solid-phase materials, a second propelling screw 11, a solid-phase material pipeline 12 and a servo motor 13, wherein one side of the solid-phase material pipeline 12 is connected with the hopper 10, the other side of the solid-phase material pipeline 12 is connected with a first feeding hole 111 through a pipeline 400, the second propelling screw 11 is arranged in the solid-phase material pipeline 12, and the servo motor 13 is electrically connected with a controller 200 and used for driving the second propelling screw 11 to push the solid-phase materials and send the solid-phase materials into a processing pipeline 101.

The second feeding unit 2 comprises at least one second dosing tank 20 for placing the aqueous phase material and a second metering pump 21, the second dosing tank 20 being connected to the second feed inlet 112 via a line 400, the second metering pump 21 being arranged on the line 400 for controlling the flow rate of the aqueous phase material into the processing line 101.

The third feeding unit 3 comprises at least one third batching tank 30 for placing the aqueous phase functional material and a third metering pump 31, the third batching tank 30 is connected with the third feeding port 113 through a pipeline 400, and the third metering pump 31 is arranged on the pipeline 400 and used for controlling the flow rate of the aqueous phase functional material into the processing pipeline 101.

The fourth feeding unit 4 comprises at least one fourth dosing tank 40 for placing oil-phase functional materials and a fourth metering pump 41, the fourth dosing tank 40 is connected with a fourth feeding port 114 through a pipeline 400, and the fourth metering pump 41 is arranged on the pipeline 400 and used for controlling the flow rate of the oil-phase functional materials entering the processing pipeline 101.

The fifth feeding unit 5 comprises at least one fifth dosing tank 50 for placing further ingredients and a fifth dosing pump 51, the fifth dosing tank 50 being connected via a line 400 to a fifth feed opening 115 in the process line 101, the fifth dosing pump 51 being arranged on the line 400 for controlling the flow rate of the further ingredients into the process line 101.

Wherein, all be provided with agitating unit 6 in second batching jar 20, third batching jar 30, fourth batching jar 40 and the fifth batching jar 50, agitating unit 6 includes the puddler 61 of being connected with agitator motor 60 and agitator motor 60 that is connected with the controller 200 electricity, and agitator motor 60 drive puddler 61 carries out the stirring to the different kinds of materials in the batching jar, carries out preliminary misce bene with the material. In addition, the second, third, fourth and fifth mix tanks 20, 30, 40 and 50 each have a heating function.

The outer sides of the second, third, fourth and fifth batch tanks 20, 30, 40 and 50 are provided with tank jackets 7, and each tank jacket 7 is provided with a third temperature sensor 70, the third temperature sensor 70 being electrically connected to the controller 200 for monitoring the temperature of each batch tank.

The pipe 400 outside is provided with the pipe box 401, form heat preservation cavity 402 between pipe box 401 and the pipe 400, the pipe box 401 outside is provided with hot water tank 403 and hot-water pump 404, hot-water tank 403, hot-water pump 404 and heat preservation cavity 402 intercommunication each other, hot-water tank 403 has self-heating function, hot-water pump 404 and controller 200 are connected and are used for driving hot water to circulate in heat preservation cavity 402 and hot-water tank 403 to reach the purpose of heat preservation pipe 400, the quantity of hot-water pump 404 of hot-water tank 403 can independently set up respectively according to the requirement of different pipe 400 to the temperature.

The human-computer interface 600 may display the temperature value detected by the temperature sensor, the pressure value detected by the pressure sensor 106, and the rotational speed of each motor, or may set the power of the hot water pump and the rotational speed of each motor. The discharging rate is adjusted according to the proportion of materials in the formula by adopting a digital automatic mode, so that the process of glue solution preparation is simplified, the data of the glue solution preparation process is clearer, the adjusting mode is more controllable, and the time and labor cost is saved.

As shown in fig. 5, a method for preparing a water-soluble glue solution according to an embodiment of the utility model is characterized by comprising the following steps:

step S1: the total materials required by the preparation of the hydrosol are classified according to the material characteristics, and the classified materials are respectively configured into each feeding station 300 of the preparation system of the hydrosol according to the material characteristics for standby.

The step S1 specifically comprises the following steps:

step S10: classifying the total materials required by the preparation of the hydrosol into solid-phase materials, water-phase efficacy materials, oil-phase efficacy materials and other ingredients according to the characteristics of the materials;

step S11: simultaneously, the solid phase material is configured to a first feeding unit 1, the water phase material is configured to a second feeding unit 2, the water phase efficacy material is configured to a third feeding unit 3, the oil phase efficacy material is configured to a fourth feeding unit 4, and other ingredients are configured to a fifth feeding unit 5;

Step S12: each feeding unit is used for standby according to the material property of each material.

Step S2: the heating system of the hydrocolloid solution preparation system is turned on to preheat the processing pipeline 101 of the shearing mixing device 100, so that the temperature in the processing pipeline 101 meets the processing requirement of the hydrocolloid solution.

Specifically, the electromagnetic infrared heater 104 is turned on to preheat the processing pipeline 101 of the shearing mixing device 100; whether the temperature in the processing pipeline 101 meets the processing requirement of the water soluble liquid is judged in real time through the first temperature sensor 107: if the first temperature sensor 107 detects that the temperature value is lower than the preset minimum value, the electromagnetic infrared heater 104 continuously heats the processing pipeline 101 of the shearing equipment 100, and if the first temperature sensor 107 detects that the temperature value is higher than the preset maximum value, the heating is stopped; the temperature in the process line 101 is controlled to be within a temperature range required for processing the hydrosol.

Step S3: the flow rate of the material of each material property into the process line 101 is calculated and configured.

The step S3 specifically comprises the following steps:

step S30: accounting the flow rate of the materials with each material property into the processing pipeline 101;

specifically, the discharge flow rate of the discharge port 110 of the process piping 110 is defined as V _{Out of} ，V _{Out of} In the range of 50-300kg/h;

the flow rates of the various materials into the process line 101 satisfy the following conditions:

V _a ＝V _{out of} ×a；

V _b ＝V _{Out of} ×b；

V _c ＝V _{Out of} ×c；

V _d ＝V _{Out of} ×d；

Ve＝V _{Out of} ×e；

Wherein V is _a 、V _b 、V _c 、V _d 、V _e The flow rates of the solid phase material, the water phase effect material, the oil phase effect material and other ingredients entering the processing pipeline 101 are respectively; a. b, c, d, e the mass ratio of solid phase material, water phase effect material, oil phase effect material and other ingredients in the total material is respectively.

Step S31: the calculated material flow rate values for each material property are configured into the respective feed stations 300.

The control of the proportion of various materials required by the water-soluble glue solution is completed by controlling the flow rate of various materials, and compared with the traditional method of controlling the proportion of the materials by manual weighing, the method has higher efficiency.

Step S4: the mixing and shearing apparatus 100 of the aqueous gel solution preparation system is started, the respective feeding stations 300 are synchronously opened, each material is conveyed into the processing pipeline 101 according to the configured flow rate, and the first screw 102 in the processing pipeline 101 simultaneously mixes and shears all the materials to obtain uniform aqueous gel solution.

The step S4 specifically comprises the following steps:

step S40: starting the shearing equipment 100 of the aqueous gel solution preparation system, and synchronously opening each feeding station 300;

Step S41: the solid phase material and the water phase material enter the processing pipeline 101 from the upstream end 116 of the processing pipeline 101, and are primarily sheared and mixed under the action of the first screw 102 and then conveyed to the downstream end 117 of the processing pipeline 101;

step S42: the water phase functional material, the oil phase functional material and other ingredients enter the processing pipeline 101 from the downstream end 117 of the processing pipeline 101, are primarily mixed with the solid phase material and water phase material mixture of the upstream end 116, and are further conveyed towards the direction of the discharge outlet 110;

step S43, shearing and mixing the water-phase functional material, the oil-phase functional material and other ingredients with the mixture of the solid-phase material and the water-phase material again, and discharging the mixture from the processing pipeline 101;

step S44: the solid phase materials, the water phase effect materials, the oil phase effect materials and other ingredients which are not fully and uniformly mixed in the processing pipeline 101 at the earlier stage of the operation of the rejection mixing and shearing equipment 100;

step S45: a uniform aqueous sol solution is obtained at the discharge outlet 110 of the process pipe 101.

Example 1:

a preparation method of a soft candy (pectin) water-soluble glue solution specifically comprises the following steps:

step S1: the total materials required for preparing the soft candy hydrosol are classified according to the material characteristics, and the classified materials are respectively arranged in each feeding station 300 of the hydrocolloid solution preparation system according to the material characteristics for standby.

The step S1 specifically comprises the following steps:

step S10: the total materials required for preparing the soft candy water-soluble glue solution are classified into solid-phase materials, water-phase efficacy materials, oil-phase efficacy materials and other ingredients according to the material characteristics, and the specific classification is shown in the following table 1.

Table 1 table of total material classification required for gum (pectin) water-soluble solutions

The temperature of various materials belongs to the prior art in the field of soft candy processing, is not particularly limited herein, and is suitable for making according to processing requirements.

The step S3 specifically comprises the following steps:

specifically, the discharge flow rate of the discharge port 110 of the process piping 110 is defined as V _{Out of} ，V _{Out of} 200kg/h.

The flow rates of the various materials in the total material required for the gum (pectin) water-soluble solution into the processing line 101 meet the following conditions, see table 2 below.

TABLE 2 flow Rate of various materials in total materials required for Water soluble gum (pectin)

The step S4 specifically comprises the following steps:

in step S43, the mixture of the aqueous phase functional material, the oil phase functional material and other ingredients, the solid phase material and the aqueous phase material is sheared and mixed again, and then discharged from the processing pipeline 101.

Step S44: the solid phase material, the water phase effect material, the oil phase effect material and other ingredients which are not fully and uniformly mixed in the processing pipeline 101 are discarded in the earlier stage of the operation of the shearing device 100.

Example 2: the preparation method of the water-soluble glue solution of soft sweets (gelatin) is different from that of the embodiment 1 in that the specific materials with each material property are different, the flow rates of the materials entering the processing pipeline 101 are not uniform, and the rest processes are uniform, which is not described in detail herein.

The total materials required for the water soluble glue solution of soft sweets (gelatin) are classified according to the material characteristics as shown in the following table 3:

table 3 table of total material classification required for gum (gelatin) aqueous solutions

Defining the discharge outlet of process piping 110110 with a discharge flow rate of V _{Out of} ，V _{Out of} 200kg/h.

The flow rates of various materials in the total material required for the gum (gelatin) aqueous solution into the processing pipe 101 satisfy the following conditions, see table 4 below.

TABLE 4 flow Rate of various materials in total materials required for Water soluble gum (gelatin) solutions

Mixture name	Ratio in total material (%)	Flow rate (kg/h)	Satisfies the condition
				Solid phase material	36.530	73.060	V _A ＝200×36.530％
Aqueous phase material	57.219	114.438	V _B ＝200×57.219％
				Aqueous phase functional material	0.874	1.748	V _C ＝200×0.874％
Oil phase functional material	2.034	4.068	V _D ＝200×2.034％
				Other ingredients	3.343	6.686	V _E ＝200×3.343％

Example 3: compared with the embodiment 1, the preparation method of the water soluble glue solution of soft sweet (carrageenan) is mainly different in specific material of each material property, and the flow rate of each material entering the processing pipeline 101 is inconsistent, and the rest processes are consistent, which is not described in detail herein.

The total materials required for the soft sweet (carrageenan) water soluble glue solution are classified according to the material properties and are shown in the following table 5:

table 5 table of total material classification required for gum (carrageenan) water soluble solutions

Defines a discharge flow rate V of the discharge port 110 of the process piping 110 _{Out of} ，V _{Out of} 200kg/h.

The flow rates of various materials in the total material required for the gum (carrageenan) aqueous solution into the processing pipeline 101 satisfy the following conditions, see table 6 below.

TABLE 6 flow Rate of various materials in total materials required for Water soluble gum (carrageenan)

Mixture name	Ratio in total material (%)	Flow rate (kg/h)	Satisfies the condition
				Solid phase material	33.62	67.240	V _A ＝200×33.62％
Aqueous phase material	61.234	122.468	V _B ＝200×61.234％
				Aqueous phase functional material	0.993	1.986	V _C ＝200×0.993％
Oil phase functional material	1.153	2.306	V _D ＝200×1.153％
				Other ingredients	3.000	6.000	V _E ＝200×3.000％

Example 4: compared with the embodiment 1, the preparation method of the water-soluble glue solution of the soft capsule rubber is mainly different in specific materials with different material properties, inconsistent in flow rate of various materials entering the processing pipeline 101, and consistent in other processes, which are not described in detail herein.

The total materials required by the water soluble glue solution of the soft capsule rubber are classified according to the material properties, and the total materials are shown in the following table 7:

table 7 total materials classification table for soft capsule skin water soluble glue solution

Defines a discharge flow rate V of the discharge port 110 of the process piping 110 _{Out of} ，V _{Out of} 250kg/h.

The flow rates of various materials in the total materials required for the soft capsule skin water-soluble liquid into the processing pipeline 101 meet the following conditions, see table 8 below.

Table 8 flow rates of various materials in total materials required for soft capsule skin water-soluble gel solution

The utility model has the following beneficial effects:

The foregoing examples illustrate only a few embodiments of the utility model and are described in detail herein without thereby limiting the scope of the utility model. It should be noted that it will be apparent to those skilled in the art that several variations and modifications can be made without departing from the spirit of the utility model, which are all within the scope of the utility model. Accordingly, the scope of protection of the present utility model is to be determined by the appended claims.

Claims

1. The utility model provides a preparation system of hydrosol liquid, its characterized in that includes mixing shear device (100), controller (200) and a plurality of feed station (300), and a plurality of feed station (300) are used for depositing the material of different material properties respectively, and a plurality of feed station (300) all are connected with mixing shear device (100) and carry the material of different material properties into mixing shear device (100), controller (200) and a plurality of feed station (300) are connected and control the speed that a plurality of feed stations (300) carried the material respectively, controller (200) with mixing shear device (100) electricity is connected and control the operation of mixing shear device (100), mixing shear device (100) are used for carrying out simultaneously to the material of different material properties and mix and shear in order to obtain the hydrocolloid solution.

2. The system for preparing an aqueous sol liquid according to claim 1, wherein the shearing apparatus (100) comprises a processing pipeline (101), a first screw (102) and a driving motor (103), the feeding station (300) is communicated with the processing pipeline (101) and is used for conveying materials with different material properties into the processing pipeline (101), the first screw (102) is arranged in the processing pipeline (101), the driving motor (103) and the controller (200) are electrically connected and are used for driving the first screw (102) to mix and shear all the materials in the processing pipeline (101) simultaneously to obtain the aqueous sol liquid, and the first screw (102) discharges the obtained aqueous sol liquid from a discharge outlet (110) of the processing pipeline (101).

3. The system for preparing an aqueous sol liquid according to claim 2, characterized in that said plurality of feeding stations (300) comprises a first feeding unit (1) for storing solid phase material and a second feeding unit (2) for storing aqueous phase material, said first feeding unit (1) and second feeding unit (2) being both in communication with said processing conduit (101) through a pipe (400).

4. A system for preparing a water-soluble liquid according to claim 3, characterized in that said plurality of feeding stations (300) further comprises a third feeding unit (3) for storing an aqueous phase functional material and a fourth feeding unit (4) for storing an oil phase functional material, said third feeding unit (3) and fourth feeding unit (4) being both in communication with said processing pipe (101) through a pipe (400).

5. The system for preparing a water-soluble liquid according to claim 4, wherein a first feed port (111) and a second feed port (112) are provided at one end of the processing pipe (101) close to the driving motor (103), a third feed port (113) and a fourth feed port (114) are provided at one end of the processing pipe (101) close to the discharge port (110), the first feed port (111) is connected to the first feed unit (1), the second feed port (112) is connected to the second feed unit (2), the third feed port (113) is connected to the third feed unit (3), and the fourth feed port (114) is connected to the fourth feed unit (4).

6. The system for preparing an aqueous sol liquid according to claim 5, wherein the first feeding unit (1) comprises a hopper (10) for storing solid phase material, a second propelling screw (11), a solid material pipe (12) and a servo motor (13), wherein one side of the solid material pipe (12) is connected with the hopper (10), the other side is connected with the first feeding port (111) through a pipe (400), the second propelling screw (11) is arranged in the solid material pipe (12), and the servo motor (13) and the controller (200) are electrically connected for driving the second propelling screw (11) to propel the solid phase material and send the solid phase material into the processing pipe (101).

7. The system for preparing an aqueous sol liquid according to claim 5, characterized in that the second feeding unit (2) comprises at least one second dosing tank (20) for placing an aqueous phase material and a second metering pump (21), the second dosing tank (20) being connected to the second feeding port (112) by means of a pipe (400), the second metering pump (21) being arranged on the pipe (400) for controlling the flow rate of the aqueous phase material into the processing pipe (101).

8. The system for preparing an aqueous sol liquid according to claim 5, characterized in that the third feeding unit (3) comprises at least one third dosing tank (30) for placing an aqueous phase efficacy material and a third metering pump (31), the third dosing tank (30) being connected to the third feeding port (113) by a pipe (400), the third metering pump (31) being arranged on the pipe (400) for controlling the flow rate of the aqueous phase efficacy material into the processing pipe (101).

9. The system for preparing an aqueous sol liquid according to claim 5, wherein the fourth feeding unit (4) comprises at least one fourth dosing tank (40) for placing oil phase efficacy materials and a fourth metering pump (41), the fourth dosing tank (40) is connected with the fourth feeding port (114) through a pipeline (400), and the fourth metering pump (41) is arranged on the pipeline (400) for controlling the flow rate of the oil phase efficacy materials into the processing pipeline (101).

10. The system for preparing an aqueous sol according to claim 5, wherein the first screw (102) comprises a plurality of sets of advancing sections (121) and shearing sections (122), the advancing sections (121) and shearing sections (122) being spaced apart from each other.

11. The system for preparing an aqueous sol liquid according to claim 10, wherein the first feed port (111), the second feed port (112), the third feed port (113) and the fourth feed port (114) and each correspond to a position of a push section (121) within the process pipe (101).

12. The system for preparing an aqueous sol liquid according to claim 11, wherein the first feed port (111) and the second feed port (112) correspond to the same segment of the pushing section (121) in the process pipe (101), and the third feed port (113) and the fourth feed port (114) correspond to the same segment of the pushing section (121) in the process pipe (101).

13. The system for preparing an aqueous sol according to claim 12, characterized in that the portion of the first screw (102) located between the second feed opening (112) and the third feed opening (113) is provided with at least one set of said shearing segments (122).

14. The system for preparing an aqueous sol according to claim 12, characterized in that the portion of the first screw (102) located between the third feed opening (113) and the discharge opening (110) is provided with at least one set of said shearing segments (122).

15. The system for preparing the hydrosol of claim 12, wherein the pushing section (121) is formed by combining a plurality of groups of pushing thread modules (123), the shearing section (122) is formed by combining a plurality of groups of shearing thread modules (124), the pitch d1 of the pushing thread modules (123) of the pushing section (121) is 36-112mm, and the pitch d2 of the shearing thread modules (124) of the shearing section (122) is 22-96mm.

16. The system for preparing an aqueous sol liquid according to claim 12, wherein said plurality of feeding stations (300) further comprises a fifth feeding unit (5) for storing other ingredients, said fifth feeding unit (5) comprising at least one fifth dosing tank (50) for placing other ingredients and a fifth metering pump (51), said fifth dosing tank (50) being connected by a pipe (400) and a fifth feeding port (115) on said processing pipe (101), said fifth feeding port (115) and said third feeding port (113) corresponding to the same section of said pushing section (121) in the processing pipe (101), said fifth metering pump (51) being arranged on the pipe (400) for controlling the flow rate of other ingredients into the processing pipe (101).