CN216878898U

CN216878898U - High viscosity polymer's feed arrangement

Info

Publication number: CN216878898U
Application number: CN202122836716.3U
Authority: CN
Inventors: 张丙伍; 朱洁; 陈星宇; 丁洺慧
Original assignee: Jiangsu Shuangjiang Energy Technology Co ltd
Current assignee: Jiangsu Shuangjiang Energy Technology Co ltd
Priority date: 2021-11-18
Filing date: 2021-11-18
Publication date: 2022-07-05
Anticipated expiration: 2031-11-18

Abstract

A high-viscosity polymer feeding device is characterized in that a fixed seat is connected to a screw rod on one side of the outer wall of a support, a weighing plate is connected to a screw rod on the outer wall of the top end of the support, a tray is arranged on the outer wall of the weighing plate, which is far away from the fixed seat, a tank body is placed on the inner wall of the tray, a funnel is connected to the screw rod on the outer wall of the top end of the fixed seat, a telescopic rod is connected to the screw rod on one side of the outer wall of the fixed seat, and a vibrating plate is arranged in the tray, so that the problems that in the prior art, a high-temperature heating method is adopted by most common feeding devices, the thermal oxidation stability of a viscosity index improver or an anti-splashing agent is influenced and the anti-yellowing risk of products is increased are solved through the weighing plate, the problems that most common feeding devices in the prior art are not provided with weighing devices and cannot accurately control are solved through the vibrating plate and a top bag, the polymer with high viscosity is not easy to discharge.

Description

High viscosity polymer's feed arrangement

Technical Field

The utility model relates to the technical field of chemical fiber oiling agents and lubricating oil, in particular to a feeding device for a high-viscosity polymer.

Background

The viscosity index improver commonly used for lubricating oil or the anti-splashing agent used in spinning oil agent is a high molecular weight polymer, although the polymer is diluted by low-viscosity industrial white oil or base oil, the viscosity of the polymer is still very large and is in a viscous semi-fluid state at normal temperature, and high-temperature steam is generally adopted for heating during industrial production to reduce the viscosity and increase the fluidity, and then the polymer is pumped into a blending tank by a pump.

Leading to ordinary feed arrangement among the prior art and adopting the method of high temperature heating mostly, can influencing viscosity index improver or anti thermal oxidation stability of splashing agent, increase the anti-yellowing's of product risk, ordinary feed arrangement does not have weighing device mostly among the prior art simultaneously, and unable accurate accuse volume, secondly ordinary feed arrangement does not have supplementary row of material structure mostly among the prior art, and high sticky polymer is difficult for discharging.

SUMMERY OF THE UTILITY MODEL

The technical problem to be solved by the utility model is as follows: in the prior art, most common feeding devices adopt a high-temperature heating method, which can affect the thermal oxidation stability of the viscosity index improver or the anti-splashing agent and increase the risk of yellowing resistance of products.

The technical scheme adopted by the utility model for solving the technical problem is as follows: a high viscosity polymer feed apparatus comprising: the support, support outer wall one side screw rod is connected with the fixing base, support top outer wall screw rod is connected with the weighing plate, the weighing plate is kept away from fixing base one side outer wall and is equipped with the tray, the jar body has been placed to the tray inner wall, fixing base top outer wall screw rod is connected with the funnel, fixing base outer wall one side screw rod is connected with the telescopic link, the inside vibrations board that is equipped with of tray, vibrations board promotion polymer flow when carrying out accurate accuse volume through the weighing plate.

As a preferable technical scheme of the utility model, one side of the outer wall of the tank body is in threaded connection with a discharge valve, the inner wall of the tank body is in sliding connection with a top bag, the outer wall of the top end of the top bag is in threaded connection with an air tap, the outer wall of the top end of the top bag is in rotary connection with a pull handle, and the polymer is discharged in an auxiliary manner through the top bag.

According to a preferable technical scheme of the utility model, the output end of the telescopic rod is rotatably connected with a rotary table, one end of the rotary table, far away from the telescopic rod, is connected with a motor through a screw rod, the output end of the motor is provided with a stirring rod, one side of the rotary table, close to the funnel, is in threaded connection with a nozzle, one side of the outer wall of the rotary table is in threaded connection with a hose, the nozzle is communicated with the hose, and the stirring rod is used for stirring white oil sprayed out through a spray head in advance to reduce the viscosity of the polymer.

According to the preferable technical scheme, a screw pump is arranged in the hopper, an output pipeline is connected to the output end of the screw pump in a threaded mode, a blending tank is connected to the outer wall of the top end of the fixing seat through a screw, the blending tank is communicated with the output pipeline, and the shearing effect of the pump on high polymers is reduced through the screw pump.

The utility model has the following advantages: the method that leads to ordinary feed arrangement and adopt high temperature heating mostly has been solved through motor and puddler among the prior art, can influence the thermal oxidation stability of viscosity index improver or anti splash agent, increase the problem of the anti yellowing risk of product, it does not have weighing device mostly to have solved ordinary feed arrangement among the prior art through the weighing plate, the problem of unable accurate accuse volume, it does not have supplementary row material structure mostly to have solved ordinary feed arrangement among the prior art through vibrations board and top bag, the difficult discharged problem of polymer of high viscosity.

Drawings

FIG. 1 is a schematic sectional front view of a main body of a feeding apparatus for a high viscosity polymer according to a preferred embodiment of the present invention;

FIG. 2 is a side cross-sectional view of a telescoping rod of a high viscosity polymer feeding device according to a preferred embodiment of the present invention;

fig. 3 is a schematic top view of a high viscosity polymer feeding device according to a preferred embodiment of the present invention.

Description of reference numerals: 1. a support; 2. a fixed seat; 3. a weighing plate; 4. a tray; 5. a tank body; 6. a funnel; 7. a telescopic rod; 8. a vibration plate; 9. ejecting a bag; 10. pulling a handle; 11. an air tap; 12. a turntable; 13. a motor; 14. a stirring rod; 15. a spout; 16. a discharge valve; 17. a screw pump; 18. and (4) a blending tank.

Detailed Description

The technical scheme of the utility model is clearly and completely described in the following with reference to the accompanying drawings. In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc., indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplicity of description, but do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying a relative importance.

In the description of the present invention, it should be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, e.g., as meaning either a fixed connection, a removable connection, or an integral connection; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.

The utility model will be further explained with reference to the drawings.

Referring to fig. 1-3, a feeding device for high viscosity polymer comprises: support 1, 1 outer wall one side screw rod of support is connected with

fixing base

2, 1 top outer wall screw rod of support is connected with weighing plate 3 for realize the function of accurate accuse volume, weighing plate 3 is kept away from 2 outer walls of one side of fixing base and is equipped with tray 4, the jar body 5 has been placed to tray 4 inner wall, 2 top outer wall screw rods of fixing base are connected with

funnel

6, 2 outer walls of fixing base one side screw rods are connected with telescopic link 7, an adjustment for realizing the height, tray 4 inside is equipped with vibrations board 8, a polymer outflow is assisted.

Wherein, output pipeline and blending tank 18 communicate each other, be used for realizing the transport function, 18 screw rods of blending tank are connected in 2 top outer walls of fixing base, be used for realizing the blending function, output pipeline threaded connection is in screw pump 17 output, 6 insides of funnel are located to screw pump 17, reduce the shearing action of pump to the high polymer through screw pump 17, draw 10 to rotate to connect in 9 top outer walls of top bag, conveniently take out the clearance after using up, air cock 11 threaded connection is in 9 top outer walls of top bag, be used for realizing compressed gas's entering, 9 sliding connection of top bag are in the discharge that 5 inner walls of the jar body are used for supplementary polymer, 16 threaded connection of discharge valve is in 5 outer walls of the jar body one side, be used for realizing row material function.

Wherein, hose and 15 intercommunications of spout for spout industry white oil in advance, hose threaded connection is in 12 outer wall one side of revolving stage, be used for carrying industry white oil, spout 15 threaded connection is in 12 one sides that are close to funnel 6 of revolving stage, be used for injecting industry white oil into funnel 6, motor 13 output is located to puddler 14, be used for realizing stirring dilution function, motor 13 screw rod is connected and is kept away from 7 one end of telescopic link in revolving stage 12, be used for stirring required power, revolving stage 12 rotates and connects in 7 outputs of telescopic link, be used for realizing angle modulation function.

Specifically, when the high polymer blending tank is used, the high polymer tank body 5 is placed on the tray 4 through a forklift, the weighing plate 3 is flatly placed on the outer wall of the top end of the support 1, the position of the discharge valve 16 is 6 ten centimeters higher than that of the hopper, then the rotary table 12 is rotated, the stirring rod 14 of the rotary table 12 is placed at the upper end of the hopper 6, stirring is carried out through transmission of the motor 13, the screw pump 17 below the hopper 6 is directly connected with the blending tank 18 through a pipeline, stirred high polymer dilution liquid directly enters the blending tank through the screw pump 17, the shearing action of the pump on high polymers is reduced after the screw pump 17 is adopted, heating is not needed, the polymers are fully dissolved in industrial white oil through gravity and stirring action, the viscosity is reduced, the high polymer blending tank is very easy to pump into blended products, energy is saved, and the risk of yellowing of anti-splash agents for thermal oxidation or textile auxiliaries of the high polymers is reduced.

The foregoing is only a preferred embodiment of the present invention, and it should be noted that those skilled in the art can make various improvements and modifications without departing from the principle of the present invention, and these improvements and modifications should also be construed as the protection scope of the present invention.

Other parts of the utility model not described in detail are prior art and are not described in detail herein.

Finally, it should be noted that: the above embodiments are only used to illustrate the technical solution of the present invention, and not to limit the same; while the utility model has been described in detail and with reference to the foregoing embodiments, it will be understood by those skilled in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some or all of the technical features may be equivalently replaced; and the modifications or the substitutions do not make the essence of the corresponding technical solutions depart from the scope of the technical solutions of the embodiments of the present invention.

Claims

1. A feeding device for high viscosity polymers, comprising: support (1), support (1) outer wall one side screw rod is connected with fixing base (2), support (1) top outer wall screw rod is connected with weighing plate (3), weighing plate (3) are kept away from fixing base (2) one side outer wall and are equipped with tray (4), the jar body (5) have been placed to tray (4) inner wall, fixing base (2) top outer wall screw rod is connected with funnel (6), fixing base (2) outer wall one side screw rod is connected with telescopic link (7), tray (4) inside is equipped with vibrations board (8).

2. The feeding device for high viscosity polymer as claimed in claim 1, wherein a discharge valve (16) is screwed on one side of the outer wall of the tank body (5), a top bag (9) is slidingly connected on the inner wall of the tank body (5), an air tap (11) is screwed on the outer wall of the top end of the top bag (9), and a pull handle (10) is rotatably connected on the outer wall of the top end of the top bag (9).

3. The feeding device for high viscosity polymers according to claim 1, characterized in that the output end of the telescopic rod (7) is rotatably connected with a rotary table (12), one end of the rotary table (12) far away from the telescopic rod (7) is connected with a motor (13) through a screw rod, the output end of the motor (13) is provided with a stirring rod (14), one side of the rotary table (12) close to the funnel (6) is connected with a nozzle (15) through a thread, one side of the outer wall of the rotary table (12) is connected with a hose through a thread, and the nozzle (15) is communicated with the hose.

4. The feeding device for high viscosity polymer according to claim 1, wherein a screw pump (17) is arranged inside the hopper (6), an output pipeline is connected to the output end of the screw pump (17) in a threaded manner, a blending tank (18) is connected to the outer wall screw at the top end of the fixed seat (2), and the blending tank (18) is communicated with the output pipeline.