A synthetic tank for the production of organic silicon emulsion phase inversion for textiles

Abstract

The utility model relates to the technical field of emulsion phase transition, and proposes a synthetic tank for phase transition production of organic silicon emulsion for textiles, including a synthetic tank body and a raw material tank, wherein the raw material tank is arranged outside the synthetic tank body, the feed assembly is arranged between the synthetic tank body and the raw material tank, the hot mixing assembly is arranged on the synthetic tank body, the vertical frame is fixed on the outer surface of the synthetic tank body, a vertical screw is installed in the vertical frame, a driving motor is arranged on the top of the vertical frame, the output end of the driving motor is connected to the vertical screw, a pair of slideways are arranged in the vertical frame, a base is slidably connected to the slideway, and the base is connected to the vertical screw by threaded matching. Through the above technical scheme, the existing technology in the related art is solved, in the organic silicon emulsification process, the organic silicon raw materials added are all organic silicon filled in the barrel, and it is inconvenient and less practical to add raw materials into the synthetic tank.

Description

Technical Field

[0001] The utility model relates to the technical field of emulsion phase inversion production, and specifically relates to an organic silicon emulsion phase inversion production synthesis tank for textiles. Background Art

[0002] Silicone emulsion (abbreviated as silicone emulsion) is an oil-in-water type emulsion composed of silicone oil, water and surfactants. In the prior art, the phase inversion production of silicone emulsion requires the emulsification of silicone, which is carried out in a synthesis tank. The silicone emulsion is emulsified by rotating and heating to obtain the required silicone emulsion.

[0003] In the existing technology, in the process of organosilicon emulsification, the organosilicon raw materials added are all organosilicon filled in the barrel, which is inconvenient and poor in practicality when adding the raw materials into the synthesis tank.

[0004] Therefore, improvements are made to address the above problems. Utility Model Content

[0005] The utility model provides a synthesis tank for phase transfer production of organic silicon emulsion for textiles, which solves the problem in the prior art of the related art that in the organic silicon emulsification process, the organic silicon raw materials added are all organic silicon filled in a barrel, which is inconvenient and has poor practicality when adding raw materials into the synthesis tank.

[0006] The technical solution of the utility model is as follows: a synthetic tank for phase inversion production of organic silicon emulsion for textiles, characterized in that it includes

[0007] A synthesis tank body and a raw material tank, wherein the raw material tank is arranged outside the synthesis tank body;

[0008] A feed assembly, the feed assembly being arranged between the synthesis tank body and the raw material tank;

[0009] A heat mixing assembly, wherein the heat mixing assembly is arranged on the synthesis tank body;

[0010] The feeding assembly includes a vertical frame, which is fixed to the outer surface of the synthesis tank body. A vertical screw is installed in the vertical frame. A driving motor is arranged on the top of the vertical frame. The output end of the driving motor is connected to the vertical screw. A pair of slides are arranged in the vertical frame. A base is slidably connected to the slides. The base is connected to the vertical screw through threaded fitting.

[0011] As a further technical solution, a circular groove is provided on the surface of the base, the raw material tank is placed in the circular groove, a feeder is provided on the surface of the synthesis tank body, a circular hole is provided on the top of the feeder, and a feeding cavity is provided inside the feeder.

[0012] As a further technical solution, a suction pipe is provided on the top of the feeder, the lower end of which is inserted into the raw material tank, and a fixing plate is provided on the outer surface of the synthesis tank body, on which a suction device is installed.

[0013] As a further technical solution, an external pipe is arranged on the top of the synthesis tank body, the external pipe is connected with the interior of the synthesis tank body, a filter is installed in the external pipe, a sealing cover is arranged on the top of the filter, and the output end of the suction device is connected with the external pipe.

[0014] As a further technical solution, the hot mixing assembly includes a stirring motor, which is installed on the top of the synthesis tank body. The top of the synthesis tank body is rotatably connected to a shaft rod, which is connected to the output end of the stirring motor.

[0015] As a further technical solution, a plurality of stirring rods are arranged outside the shaft rod, dispersion racks are connected between the stirring rods, a plurality of fixing rods are arranged on the inner wall of the synthesis tank body, and heating tubes are fixedly connected to the fixing rods.

[0016] As a further technical solution, the dispersion rack has an overall hexagonal rhombus structure.

[0017] As a further technical solution, the heating tube is annular in structure as a whole, and the heating tube is located in the middle part of the synthesis tank body.

[0018] As a further technical solution, the inner bottom surface of the feed cavity is an inclined structural surface.

[0019] As a further technical solution, the lower end of the suction pipe and the circular groove are located at the same axial position.

[0020] The working principle and beneficial effects of the utility model are:

[0021] The utility model is provided with a feeding assembly. Through the interaction of structures such as a vertical screw, a base, a circular groove, a feeder, a feeding chamber, suction, a suction pipe and a suction device, the inside of the synthesis tank body can be sucked to a negative pressure state by exhausting air. After the negative pressure, the suction is turned on to quickly lift the liquid in the raw material tank into the synthesis tank body. The raw material tank is controlled to rise and fall by the vertical screw and can be quickly docked, which saves a lot of manpower-operated tools and has good feeding effect and practicality. BRIEF DESCRIPTION OF THE DRAWINGS

[0022] The utility model is further described in detail below in conjunction with the accompanying drawings and specific implementation methods.

[0023] Figure 1 It is a schematic diagram of the structure of the utility model;

[0024] Figure 2 This is a cross-sectional view of the utility model;

[0025] Figure 3 This is a cross-sectional view from another perspective of the utility model;

[0026] Figure 4 For the utility model Figure 2 A partial enlarged view of part A;

[0027] In the figure: 1. synthesis tank body; 2. raw material tank; 3. feeding assembly; 3-1. vertical frame; 3-2. vertical screw; 3-3. driving motor; 3-4. slideway; 3-5. base; 3-6. circular groove; 3-7. feeder; 3-8. circular hole; 3-9. feeding chamber; 3-10. suction pipe; 3-11. fixed plate; 3-12. suction device; 3-13. external pipeline; 3-14. filter; 3-15. sealing cover; 4. hot mixing assembly; 4-1. stirring motor; 4-2. shaft; 4-3. stirring rod; 4-4. dispersion rack; 4-5. fixed rod; 4-6. heating tube. DETAILED DESCRIPTION

[0028] The following will be combined with the embodiments of the utility model to clearly and completely describe the technical solutions in the embodiments of the utility model. Obviously, the described embodiments are only part of the embodiments of the utility model, not all of the embodiments. Based on the embodiments of the utility model, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the utility model.

[0029] like Figure 1~Figure 4 As shown, this embodiment proposes a textile organic silicone emulsion phase inversion production synthesis tank, including

[0030] A synthesis tank body 1 and a raw material tank 2, wherein the raw material tank 2 is arranged outside the synthesis tank body 1;

[0031] A feed assembly 3, which is arranged between the synthesis tank body 1 and the raw material tank 2;

[0032] A heat mixing assembly 4, which is arranged on the synthesis tank body 1;

[0033] The feeding assembly 3 includes a vertical frame 3-1, which is fixed to the outer surface of the synthesis tank body 1, a vertical screw 3-2 is installed in the vertical frame 3-1, a driving motor 3-3 is arranged on the top of the vertical frame 3-1, and the output end of the driving motor 3-3 is connected to the vertical screw 3-2, a pair of slideways 3-4 are arranged in the vertical frame 3-1, a base 3-5 is slidably connected to the slideway 3-4, the base 3-5 is connected to the vertical screw 3-2 by threaded matching, a circular groove 3-6 is opened on the surface of the base 3-5, the raw material tank 2 is placed in the circular groove 3-6, a feeder 3-7 is arranged on the surface of the synthesis tank body 1, and the feeder 3-7 is arranged on the top A circular hole 3-8 is provided on the part, a feeding cavity 3-9 is provided inside the feeder 3-7, a suction pipe 3-10 is provided on the top of the feeder 3-7, and the lower end of the suction pipe 3-10 is inserted in the raw material tank 2, a fixing plate 3-11 is provided on the outer surface of the synthesis tank body 1, and a suction device 3-12 is installed on the fixing plate 3-11, an external pipe 3-13 is provided on the top of the synthesis tank body 1, the external pipe 3-13 is connected with the inside of the synthesis tank body 1, a filter 3-14 is installed in the external pipe 3-13, a sealing cover 3-15 is provided on the top of the filter 3-14, and the output end of the suction device 3-12 is connected with the external pipe 3-13.

[0034] In this embodiment, in order to achieve the effect of feeding by suction, a feeding assembly 3 is designed, a vertical frame 3-1 is arranged on the outer surface of the synthesis tank body 1, a vertical screw 3-2, a driving motor 3-3 and a slide 3-4 are arranged in the vertical frame 3-1, the driving motor 3-3 is used to control the rotation of the vertical screw 3-2, a base 3-5 is connected to the vertical screw 3-2 and the slide 3-4, a circular groove 3-6 is provided on the surface of the base 3-5 for placing the raw material tank 2, a feeder 3-7 is installed on the outer wall of the synthesis tank body 1, a circular hole 3-8 and a feeder 3-7 are provided in the feeder 3-7 A material cavity 3-9 is provided with a suction pipe 3-10 on the top of the feeder 3-7 and is vertically inserted into the raw material tank 2. A fixing plate 3-11 is provided on the top of the synthesis tank body 1 and a suction device 3-12 is installed. An external pipe 3-13 is also provided. The external pipe 3-13 is connected to the output end of the suction device 3-12, and can suck the gas inside the synthesis tank body 1. After evacuation, the material in the raw material tank 2 enters the synthesis tank body 1 through the feed cavity 3-9 by means of negative pressure, and a filter and a sealing cover 3-15 are installed in the external pipe 3-13 to filter the gas at the suction point.

[0035] Furthermore, the hot mixing component 4 includes a stirring motor 4-1, which is installed on the top of the synthesis tank body 1. The top of the synthesis tank body 1 is rotatably connected to a shaft rod 4-2, which is connected to the output end of the stirring motor 4-1. A plurality of stirring rods 4-3 are arranged outside the shaft rod 4-2, and a dispersion rack 4-4 is connected between the stirring rods 4-3. A plurality of fixed rods 4-5 are arranged on the inner wall of the synthesis tank body 1, and a heating tube 4-6 is fixedly connected to the fixed rod 4-5.

[0036] In this embodiment, in order to achieve the effect of uniform heating and stirring inside the synthesis tank body 1, a hot mixing component 4 is designed, and a stirring motor 4-1 is installed on the top of the synthesis tank body 1. An axle rod 4-2, a stirring rod 4-3 and a dispersion rack 4-4 are rotated inside, and stirring can be performed by controlling the stirring motor 4-1. A fixing rod 4-5 and a heating tube 4-6 are fixed on the inner wall to heat the interior.

[0037] Furthermore, the dispersion rack 4 - 4 has a hexagonal rhombus structure as a whole.

[0038] In this embodiment, a dispersed shearing effect can be achieved through the hexagonal rhombus structure.

[0039] Furthermore, the heating tube 4 - 6 is annular in structure as a whole, and the heating tube 4 - 6 is located in the middle part of the synthesis tank body 1 .

[0040] In this embodiment, the annular structure, in conjunction with the flow direction of the stirring liquid, can achieve rapid and uniform heating from the inside to the outside.

[0041] Furthermore, the inner bottom surface of the feed cavity 3-9 is an inclined structural surface.

[0042] In this embodiment, the inclined structural surface prevents the inflowing liquid from remaining in the feed cavity 3-9.

[0043] Furthermore, the lower end of the suction pipe 3-10 and the circular groove 3-6 are located at the same axial position.

[0044] In this embodiment, the coaxial position ensures that the suction tube 3 - 10 can be accurately inserted each time the raw material tank 2 is placed.

[0045] When it is necessary to process and inject raw materials, place the raw material tank 2 into the circular groove 3-6 of the base 3-5, then start the drive motor 3-3 to control the vertical screw 3-2 to rotate, so that the raw material tank 2 is vertically upward, and the suction tube 3-10 is inserted into the raw material tank 2, and then start the suction device 3-12, and the raw materials are sucked into the synthesis tank body 1 through the circular hole 3-8 of the feeder 3-7 and the feeding chamber 3-9 by negative pressure. After all the raw materials are injected, close the valve on the suction tube 3-10, and then start the stirring motor 4-1 to stir the stirring rod 4-3 and the dispersion rack 4-4, and start the heating tube 4-6 for heating.

[0046] The above are only preferred embodiments of the present invention and are not intended to limit the present invention. Any modifications, equivalent substitutions, improvements, etc. made within the spirit and principles of the present invention should be included in the protection scope of the present invention.

Claims

1. A synthetic tank for producing phase-inversion of organic silicon emulsion for textiles, characterized in that: include A synthesis tank body (1) and a raw material tank (2), wherein the raw material tank (2) is arranged outside the synthesis tank body (1); A feed assembly (3), wherein the feed assembly (3) is arranged between the synthesis tank body (1) and the raw material tank (2); A heat mixing assembly (4), wherein the heat mixing assembly (4) is arranged on the synthesis tank body (1); The feeding assembly (3) comprises a vertical frame (3-1), the vertical frame (3-1) is fixed to the outer surface of the synthesis tank body (1), a vertical screw (3-2) is installed in the vertical frame (3-1), a driving motor (3-3) is arranged on the top of the vertical frame (3-1), the output end of the driving motor (3-3) is connected to the vertical screw (3-2), a pair of slideways (3-4) is arranged in the vertical frame (3-1), a base (3-5) is slidably connected to the slideway (3-4), and the base (3-5) is connected to the vertical screw (3-2) by threaded matching.

2. The organic silicon emulsion phase inversion production synthesis tank for textiles according to claim 1, characterized in that: A circular groove (3-6) is provided on the surface of the base (3-5), the raw material tank (2) is placed in the circular groove (3-6), a feeder (3-7) is provided on the surface of the synthesis tank body (1), a circular hole (3-8) is provided on the top of the feeder (3-7), and a feed cavity (3-9) is provided inside the feeder (3-7).

3. The organic silicon emulsion phase inversion production synthesis tank for textiles according to claim 2, characterized in that: A suction pipe (3-10) is provided on the top of the feeder (3-7), and the lower end of the suction pipe (3-10) is inserted into the raw material tank (2). A fixing plate (3-11) is provided on the outer surface of the synthesis tank body (1), and a suction device (3-12) is installed on the fixing plate (3-11).

4. The organic silicon emulsion phase inversion production synthesis tank for textiles according to claim 3, characterized in that: An external pipe (3-13) is arranged on the top of the synthesis tank body (1), the external pipe (3-13) is connected with the inside of the synthesis tank body (1), a filter (3-14) is installed in the external pipe (3-13), a sealing cover (3-15) is arranged on the top of the filter (3-14), and the output end of the suction device (3-12) is connected to the external pipe (3-13).

5. The organic silicon emulsion phase inversion production synthesis tank for textiles according to claim 1, characterized in that: The heat mixing assembly (4) comprises a stirring motor (4-1), wherein the stirring motor (4-1) is mounted on the top of the synthesis tank body (1), and a shaft (4-2) is rotatably connected to the top of the synthesis tank body (1), and the shaft (4-2) is connected to the output end of the stirring motor (4-1).

6. The organic silicon emulsion phase inversion production synthesis tank for textiles according to claim 5, characterized in that: A plurality of stirring rods (4-3) are arranged outside the shaft rod (4-2), and dispersion racks (4-4) are connected between the stirring rods (4-3). A plurality of fixing rods (4-5) are arranged on the inner wall of the synthesis tank body (1), and a heating tube (4-6) is fixedly connected to the fixing rod (4-5).

7. The organic silicon emulsion phase inversion production synthesis tank for textiles according to claim 6, characterized in that: The dispersion rack (4-4) is in a hexagonal rhombus structure as a whole.

8. The organic silicon emulsion phase inversion production synthesis tank for textiles according to claim 6, characterized in that: The heating tube (4-6) is in an annular structure as a whole, and the heating tube (4-6) is located in the middle part of the synthesis tank body (1).

9. The organic silicon emulsion phase inversion production synthesis tank for textiles according to claim 3, characterized in that: The inner bottom surface of the feeding cavity (3-9) is an inclined structural surface.

10. The organic silicon emulsion phase inversion production synthesis tank for textiles according to claim 3, characterized in that: The lower end of the suction pipe (3-10) and the circular groove (3-6) are located at the same axial position.

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