CN219879758U - Spiral mixing arrangement of hydrocolloid glue - Google Patents

Spiral mixing arrangement of hydrocolloid glue Download PDF

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Publication number
CN219879758U
CN219879758U CN202321182015.5U CN202321182015U CN219879758U CN 219879758 U CN219879758 U CN 219879758U CN 202321182015 U CN202321182015 U CN 202321182015U CN 219879758 U CN219879758 U CN 219879758U
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China
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fixedly connected
hydrocolloid
spiral mixing
mixing device
heating wires
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CN202321182015.5U
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Chinese (zh)
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李华顺
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Qingdao Furuiwo New Material Co ltd
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Qingdao Furuiwo New Material Co ltd
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Abstract

The utility model provides a hydrocolloid glue spiral mixing device, which belongs to the technical field of colloid mixing devices, and comprises an operation platform, wherein a material guide pipe is fixedly connected above the operation platform, a grinding mechanism is fixedly connected above the material guide pipe, a stirring bin is fixedly connected to the bottom of the operation platform, a stirrer and a first driving motor are arranged in the stirring bin, a spiral blade is fixedly connected to the outer wall of the stirrer, an output shaft of the first driving motor is fixedly connected with a rotating shaft of the stirrer, annular material inlets are formed in the periphery of the output shaft of the first driving motor, a discharge hole is formed in the bottom of the stirrer, and a segmented temperature control mechanism is arranged in the stirrer; the utility model can solve the problem that the glue viscosity is reduced after stirring due to uneven heating of the colloid raw materials.

Description

Spiral mixing arrangement of hydrocolloid glue
Technical Field
The utility model belongs to the technical field of colloid mixing devices, and particularly relates to a hydrocolloid glue spiral mixing device.
Background
The utility model of China (application number: CN 201720654673.8) with publication number of CN207221781U provides a glue stirring and heating kettle, which comprises a kettle body, wherein a feed inlet is formed in the upper end of the kettle body, a feed cover is arranged on the feed inlet, a gas accommodating pipe communicated with the inside of the kettle body is vertically connected to the upper end of the kettle body, a cooling device is arranged outside the gas accommodating pipe and used for cooling gas evaporated into the gas accommodating pipe to flow back into the kettle body, a heating device is arranged outside the kettle body, a stirring shaft is rotatably arranged in the middle of the kettle body, stirring blades are fixedly connected to the stirring shaft, and a driving device is connected to the upper end of the stirring shaft in a transmission manner.
In the utility model, the reaction kettle is directly heated by the heating device, so that the problem that the colloid raw material is heated unevenly and the viscosity of the glue is reduced after stirring exists.
Disclosure of Invention
In view of the above, the utility model provides a spiral mixing device for hydrocolloid glue, which can solve the problem that the glue viscosity is reduced after stirring due to uneven heating of colloid raw materials.
The utility model is realized in the following way:
the utility model provides a hydrocolloid glue spiral mixing device which comprises an operation platform, wherein a material guide pipe is fixedly connected above the operation platform, a grinding mechanism is fixedly connected above the material guide pipe, a stirring bin is fixedly connected with the bottom of the operation platform, a stirrer and a first driving motor are arranged in the stirring bin, a spiral blade is fixedly connected to the outer wall of the stirrer, an output shaft of the first driving motor is fixedly connected with a rotating shaft of the stirrer, annular material inlets are formed in the periphery of the output shaft of the first driving motor, a material outlet is formed in the bottom of the stirrer, and a sectional temperature control mechanism is arranged in the stirrer.
The technical effects of the spiral mixing device for the hydrocolloid glue provided by the utility model are as follows: the colloid raw material can be ground by arranging the grinding mechanism and is sent into the material guide pipe; by arranging the sectional temperature control mechanism, the colloid raw material can be gradually warmed up in a sectional manner, so that the produced glue has high viscosity and is not easy to yellow; the glue after the colloid is melted is fully stirred and mixed by arranging the stirrer, so that the produced glue has better fluidity.
On the basis of the technical scheme, the hydrocolloid glue spiral mixing device can be improved as follows:
the grinding mechanism is internally provided with two grinding rollers, the outer part of the grinding mechanism is also provided with a second driving motor, an output shaft of the second driving motor is fixedly connected with the two grinding rollers, and the two grinding rollers are opposite in rotation direction and inward.
The beneficial effects of adopting above-mentioned improvement scheme are: through setting up the opposite and inwards rotation direction of two grinding rollers, can carry out extrusion formula grinding with the colloid raw materials, make the colloid raw materials remove to the agitator.
Further, the sectional temperature control mechanism comprises heating wires, and the distribution mode of the heating wires is that the distance from top to bottom to the rotating shaft is gradually reduced.
Further, the sectional temperature control mechanism comprises heating wires, and the distribution mode of the heating wires is that the distribution density of the heating wires is gradually dense from top to bottom.
Further, the sectional temperature control mechanism comprises heating wires, the distribution mode of the heating wires is that the distribution density is the same from top to bottom, heat conduction layers with different heat conduction rates are arranged between the heating wires and the rotating shaft, and the heat conduction rates of the heat conduction layers are gradually increased from top to bottom.
Further, the outlet of the material guide pipe is matched with the annular feeding port.
Further, the shape of the spiral blade is matched with the stirring bin.
The beneficial effects of adopting above-mentioned improvement scheme are: through set up helical blade's shape with stirring storehouse looks adaptation can stir the colloid in the whole space of stirring storehouse when the agitator stirs, makes the stirring more even.
Further, the stirrer is provided with an annular cavity, and a through hole communicated with the discharging hole is formed in the bottom of the annular cavity.
The beneficial effects of adopting above-mentioned improvement scheme are: through setting up the through-hole, can flow into the stirring storehouse inside through the discharge gate with the colloid raw materials after the heating and stir the mixing and handle.
Further, four supporting feet are arranged at the bottom of the operation platform.
Further, a discharge hole is formed in the bottom of the stirring bin, and a valve is arranged on the discharge hole.
Compared with the prior art, the hydrocolloid glue spiral mixing device provided by the utility model has the beneficial effects that: the colloid raw material can be ground by arranging the grinding mechanism and is sent into the material guide pipe; by arranging the sectional temperature control mechanism, the colloid raw material can be gradually warmed up in a sectional manner, so that the produced glue has high viscosity and is not easy to yellow; the glue after the colloid is melted is fully stirred and mixed by arranging the stirrer, so that the produced glue has better fluidity; through setting up the opposite and inwards rotation direction of two grinding rollers, can carry out extrusion formula grinding with the colloid raw materials, make the colloid raw materials remove to the agitator.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present utility model, the drawings that are needed in the description of the embodiments of the present utility model will be briefly described below, it being obvious that the drawings in the following description are only some embodiments of the present utility model, and that other drawings may be obtained according to these drawings without inventive effort for a person skilled in the art.
FIG. 1 is a schematic diagram of a spiral mixing device for hydrocolloid glue;
FIG. 2 is a rear view of a hydrocolloid adhesive screw mixer;
FIG. 3 is a schematic diagram of a mixer structure of a spiral mixing device for hydrocolloid gums;
FIG. 4 is a schematic view showing the internal structure of a first embodiment of the agitator;
FIG. 5 is a schematic view showing the internal structure of a second embodiment of the agitator;
FIG. 6 is a schematic view showing the internal structure of a third embodiment of the agitator;
in the drawings, the list of components represented by the various numbers is as follows:
10. an operating platform; 11. a grinding mechanism; 12. a material guiding pipe; 13. an annular feed inlet; 14. a rotation shaft; 15. a first driving motor; 16. a second driving motor; 17. a sectional temperature control mechanism; 18. a helical blade; 19. a discharge hole; 20. a discharge port; 21. a grinding roller; 22. a heating wire; 23. a stirring bin; 24. a support leg; 25. a stirrer; 26. and a heat conducting layer.
Detailed Description
For the purpose of making the objects, technical solutions and advantages of the embodiments of the present utility model more apparent, the technical solutions of the embodiments of the present utility model will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present utility model, and it is apparent that the described embodiments are some embodiments of the present utility model, but not all embodiments. All other embodiments, based on the embodiments of the utility model, which are apparent to those of ordinary skill in the art without inventive faculty, are intended to be within the scope of the utility model.
Thus, the following detailed description of the embodiments of the utility model, as presented in the figures, is not intended to limit the scope of the utility model, as claimed, but is merely representative of selected embodiments of the utility model. All other embodiments, based on the embodiments of the utility model, which are apparent to those of ordinary skill in the art without inventive faculty, are intended to be within the scope of the utility model.
It should be noted that: like reference numerals and letters denote like items in the following figures, and thus once an item is defined in one figure, no further definition or explanation thereof is necessary in the following figures.
In the description of the present utility model, it should be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", etc. indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings are merely for convenience in describing the present utility model and simplifying the description, and do not indicate or imply that the apparatus or elements referred to must have a specific orientation, be configured and operated in a specific orientation, and thus should not be construed as limiting the present utility model.
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 one or more such feature. In the description of the present utility model, the meaning of "a plurality" is two or more, unless explicitly defined otherwise.
As shown in fig. 1-4, in the first embodiment of the spiral mixing device for hydrocolloid glue provided by the utility model, the first embodiment comprises an operation platform 10, a material guiding pipe 12 is fixedly connected above the operation platform 10, a grinding mechanism 11 is fixedly connected above the material guiding pipe 12, a stirring bin 23 is fixedly connected to the bottom of the operation platform 10, a stirrer 25 and a first driving motor 15 are arranged in the stirring bin 23, a helical blade 18 is fixedly connected to the outer wall of the stirrer 25, an output shaft of the first driving motor 15 is fixedly connected with a rotating shaft 14 of the stirrer 25, annular material inlets 13 are formed around the output shaft of the first driving motor 15, a material outlet 19 is formed in the bottom of the stirrer 25, and a segmented temperature control mechanism 17 is arranged in the stirrer 25.
In order to prevent the stirrer 25 from being heated for a long period of time, the temperature of the entire stirrer 25 is the same throughout the stirrer 25 due to heat conduction, temperature sensors are provided at the top and bottom of the rotary shaft 14 to detect the temperatures at the upper and lower ends of the stirrer 25, and the heating is stopped when the temperature at the lower end of the stirrer 25 approaches the highest temperature (typically 125 degrees celsius) of the colloidal raw material.
In the above technical solution, two grinding rollers 21 are disposed in the grinding mechanism 11, a second driving motor 16 is further disposed outside the grinding mechanism 11, an output shaft of the second driving motor 16 is fixedly connected with the two grinding rollers 21, and the two grinding rollers 21 rotate in opposite directions and are inward.
Further, in the above technical solution, the sectional temperature control mechanism 17 includes the heating wires 22, the distribution mode of the heating wires 22 is that the distance from top to bottom to the rotating shaft 14 gradually decreases, and the same heating wires 22 far away from the rotating shaft 14 have time difference in heat conduction on the premise that the materials arranged between the rotating shaft 14 and the heating wires 22 are the same, so that the sectional temperature control mechanism 17 gradually increases the temperature from top to bottom, the colloid raw material gradually increases the temperature, and the raw material colloid is heated more uniformly.
In the second embodiment of the spiral mixing device for hydrocolloid glue provided by the present utility model, as shown in fig. 5, the sectional temperature control mechanism 17 includes the heating wires 22, the distribution mode of the heating wires 22 is that the distribution density of the heating wires becomes gradually dense from top to bottom, and on the premise that the materials arranged between the rotating shaft 14 and the heating wires 22 are the same, the larger the distribution density of the heat conducting layer 26 is, the more heat generated by the part, the gradually heating up from top to bottom is formed by the sectional temperature control mechanism 17, the gradually heating up is performed on the colloid raw material, and the raw material colloid is heated more uniformly.
As shown in fig. 6, in the third embodiment of the spiral mixing device for hydrocolloid glue provided by the present utility model, the sectional temperature control mechanism 17 includes heating wires 22, the distribution mode of the heating wires 22 is the same from top to bottom, and heat conducting layers 26 with different heat conducting rates are arranged between the heating wires 22 and the rotating shaft 14, the heat conducting rate of the heat conducting layers 26 gradually increases from top to bottom, the heat conducting rate is changed by changing the heat conducting material between the rotating shaft 14 and the heating wires 22, and gradual temperature rise from top to bottom is formed in the sectional temperature control mechanism 17, so that the colloid raw material gradually rises in temperature, and the raw material colloid is heated more uniformly.
The heat conducting material can be copper alloy, and the heat conducting rate of the copper alloy is changed by changing the content of other metals in the unit volume of the copper alloy.
Further, in the above technical solution, the outlet of the material guiding pipe 12 is adapted to the annular material inlet 13.
Further, in the above technical solution, the shape of the helical blade 18 is adapted to the stirring chamber 23.
Further, in the above technical solution, the agitator 25 is provided with an annular cavity, and a through hole communicated with the discharge hole 19 is provided at the bottom of the annular cavity.
Further, in the above technical solution, four legs 24 are provided at the bottom of the operation platform 10.
Further, in the above technical scheme, a discharge port 20 is arranged at the bottom of the stirring bin 23, and a valve is arranged on the discharge port 20.
The foregoing is merely illustrative of the present utility model, and the present utility model is not limited thereto, and any person skilled in the art will readily recognize that variations or substitutions are within the scope of the present utility model. Therefore, the protection scope of the utility model is subject to the protection scope of the claims.

Claims (10)

1. The utility model provides a hydrocolloid glue spiral mixing arrangement, includes operation platform (10), operation platform (10) top fixedly connected with feed conduit (12), feed conduit (12) top fixedly connected with grinding mechanism (11), operation platform (10) bottom fixedly connected with stirring storehouse (23), a serial communication port, be equipped with agitator (25) and first driving motor (15) in stirring storehouse (23), agitator (25) outer wall fixedly connected with helical blade (18), the output shaft of first driving motor (15) and rotation axis (14) fixed connection of agitator (25), be equipped with annular pan feeding mouth (13) around the output shaft of first driving motor (15), the bottom on agitator (25) is equipped with discharge opening (19), be equipped with segmentation temperature control mechanism (17) in agitator (25).
2. The hydrocolloid glue spiral mixing device according to claim 1, wherein two grinding rollers (21) are arranged in the grinding mechanism (11), a second driving motor (16) is further arranged outside the grinding mechanism (11), an output shaft of the second driving motor (16) is fixedly connected with the two grinding rollers (21), and the two grinding rollers (21) are opposite in rotation direction and inward.
3. The spiral mixing device for hydrocolloid glue according to claim 2, wherein the segmented temperature control mechanism (17) comprises heating wires (22), and the heating wires (22) are distributed in such a way that the distance from top to bottom to the rotating shaft (14) is gradually reduced.
4. The spiral mixing device for hydrocolloid glue according to claim 2, wherein the segmented temperature control mechanism (17) comprises heating wires (22), and the heating wires (22) are distributed in a manner that the distribution density gradually becomes dense from top to bottom.
5. The spiral mixing device for hydrocolloid glue according to claim 2, wherein the segmented temperature control mechanism (17) comprises heating wires (22), the heating wires (22) are distributed in the same density from top to bottom, heat conducting layers (26) with different heat conducting rates are arranged between the heating wires (22) and the rotating shaft (14), and the heat conducting rate of the heat conducting layers (26) is gradually increased from top to bottom.
6. A hydrocolloid gum spiral mixing device according to any one of claims 3-5, wherein the outlet of the feed conduit (12) is adapted to the annular feed opening (13).
7. A hydrocolloid gum screw mixer according to claim 6, characterised in that the shape of the screw blade (18) is adapted to the mixing chamber (23).
8. The hydrocolloid gum spiral mixing device according to claim 7, wherein the stirrer (25) is provided with an annular cavity, the bottom of which is provided with a through hole communicating with the discharge hole (19).
9. A hydrocolloid glue spiral mixing device according to claim 8, wherein four feet (24) are provided at the bottom of the operating platform (10).
10. The spiral mixing device for hydrocolloid glue according to claim 9, wherein a discharge port (20) is arranged at the bottom of the stirring bin (23), and a valve is arranged on the discharge port (20).
CN202321182015.5U 2023-05-17 2023-05-17 Spiral mixing arrangement of hydrocolloid glue Active CN219879758U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202321182015.5U CN219879758U (en) 2023-05-17 2023-05-17 Spiral mixing arrangement of hydrocolloid glue

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202321182015.5U CN219879758U (en) 2023-05-17 2023-05-17 Spiral mixing arrangement of hydrocolloid glue

Publications (1)

Publication Number Publication Date
CN219879758U true CN219879758U (en) 2023-10-24

Family

ID=88402663

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202321182015.5U Active CN219879758U (en) 2023-05-17 2023-05-17 Spiral mixing arrangement of hydrocolloid glue

Country Status (1)

Country Link
CN (1) CN219879758U (en)

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