A refining production line and production process of ethylene bis-stearamide

By designing an ethylene bis-stearamide refining production line and optimizing the equipment layout, the problems of low production efficiency and high cost caused by independent equipment were solved, achieving efficient cleaning and drying, improving production efficiency and reducing costs.

CN116674119BActive Publication Date: 2026-05-08ZHEJIANG XINSTE NEW MATERIALS CO LTD
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Patent Information

Authority / Receiving Office
CN · China
Patent Type
Patents(China)
Current Assignee / Owner
ZHEJIANG XINSTE NEW MATERIALS CO LTD
Filing Date
2023-04-13
Publication Date
2026-05-08

AI Technical Summary

Technical Problem

In the existing ethylene bis-stearamide production process, the equipment is independent and the loading and unloading are cumbersome, which affects production efficiency and cost.

Method used

A refining production line for ethylene bis-stearamide was designed, including cleaning equipment, filtration equipment, primary drying equipment and secondary drying equipment. The equipment structure is optimized by a series layout, and efficient cleaning and drying are achieved by using agitators, turning tables, conveyor belts and thermal radiation heating components.

Benefits of technology

It improved production efficiency, reduced the input of human and material resources, and lowered production costs.

✦ Generated by Eureka AI based on patent content.

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Abstract

The present application relates to a kind of ethylene bis stearamide refining production line and production process.It includes cleaning equipment, the cleaning equipment includes washing tank and stirrer, the bottom of washing tank is equipped with discharge port;Filtering equipment;Primary drying equipment, the primary drying equipment includes turnover table, drying platform on the turnover table, electric heating component in the turnover table;Secondary drying equipment, the secondary drying equipment includes receiving hopper, conveying belt below the receiving hopper and hot radiation heating component on the conveying belt path, the bottom of receiving hopper is attached with the upper surface of conveying belt, and the bottom of receiving hopper and located on the conveying belt far side is equipped with discharge gap.The present application redesigns the structure of equipment in part production, and optimizes layout, connects each production equipment in series, reduces the manpower and material resources spent on feeding and discharging.
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Description

Technical Field

[0001] This invention relates to an apparatus for producing ethylene bis-stearamide, and more particularly to a refining production line and process for ethylene bis-stearamide. Background Technology

[0002] The production process of ethylene bis-stearamide is as follows: Prepare raw materials, including ethylene amine and stearamide; mix ethylene amine and stearamide together and feed them into a reaction vessel; add a small amount of acidic catalyst (such as copper sulfate or sodium sulfate); heat the mixture in the reaction vessel to the reaction temperature (usually 60-80℃) and maintain the reaction time for 3-5 hours; discharge the mixture from the reaction vessel after the reaction is complete, wash and dry it to obtain the finished product. Currently, the preparation of ethylene bis-stearamide using a reaction vessel is a mature process, but the ethylene bis-stearamide produced by the reaction vessel is a mixture and requires refining. The current production of ethylene bis-stearamide requires a lot of independent equipment, and the loading and unloading of each piece of equipment requires manpower and resources, which significantly affects production efficiency and costs. Summary of the Invention

[0003] This invention provides a refining production line and process for ethylene bis-stearamide, solving the problem that the equipment required for the production and refining of ethylene bis-stearamide is independent in the prior art.

[0004] The above-mentioned technical problems of the present invention are mainly solved by the following technical solution: a refining production line and production process for ethylene bis-stearamide, including a cleaning device, wherein the cleaning device includes a cleaning tank and a stirrer, and the bottom of the cleaning tank is provided with a discharge port;

[0005] Filtration equipment;

[0006] A primary drying device, comprising a tilting table, a drying platform located on the tilting table, and an electric heating component located inside the tilting table;

[0007] A secondary drying device includes a receiving hopper, a conveyor belt located below the receiving hopper, and a thermal radiation heating component located on the path of the conveyor belt. The bottom of the receiving hopper is in contact with the upper surface of the conveyor belt, and a discharge notch is provided on the bottom of the receiving hopper on the side away from the conveyor belt.

[0008] The production process includes:

[0009] S1. Pour all the mixture after the chemical reaction in the reactor into the cleaning tank, add clean water into the cleaning tank and control the stirrer to rotate and stir. After stirring for a period of time, stop the stirrer and let it stand for a period of time. After draining the upper wastewater, add clean water again and repeat the above steps at least twice. Finally, obtain a cleaned mixture of ethylene bis-stearamide and water. Turn on the stirrer again and open the discharge port to discharge the ethylene bis-stearamide fluid.

[0010] S2 guides the ethylene bis-stearamide fluid discharged from S1 to the filtration equipment for filtration, and removes excess water;

[0011] S3, pour the wet ethylene bis-stearamide granules obtained in S2 onto the drying platform of the primary drying equipment, heat the drying platform with the electric heating element, and after the predetermined time is reached, the tilting table is tilted downward to pour out the ethylene bis-stearamide granules on it.

[0012] S4. Pour the ethylene bis-stearamide granules obtained in S3 into the receiving hopper. The ethylene bis-stearamide granules in the receiving hopper are output from the discharge gap along the conveyor belt, heated by the thermal radiation heating component, and then output from the conveyor belt.

[0013] This invention reduces the manpower and resources spent on loading and unloading materials by redesigning the structure of some production equipment and optimizing the layout, connecting various production equipment in series.

[0014] Furthermore, a solenoid valve is provided at the discharge port, and a discharge pipe is connected between the discharge port and the filter device, with a pumping device provided on the discharge pipe.

[0015] Furthermore, the upper side of the cleaning tank is provided with a feed inlet, a water inlet and a motor, the motor is connected to the agitator, and the bottom of the cleaning tank is also provided with an upward-extending drain pipe.

[0016] Furthermore, the filtration device includes a truss slide rail, a sliding seat slidably connected to the truss, a mounting frame fixed to the sliding seat, and a flip filter frame rotatably connected to the mounting frame. The sliding seat can move the flip filter frame along the truss slide rail to the lower side of the discharge port of the discharge pipe and the upper side of the primary drying device.

[0017] Furthermore, the flip filter frame includes a frame and a filter layer laid flat at the bottom of the frame.

[0018] Furthermore, the primary drying equipment also includes a base and a hydraulic cylinder rotatably connected to the base, the tilting table is rotatably connected to the base, and the telescopic rod of the hydraulic cylinder is rotatably connected to the bottom of the tilting table.

[0019] Furthermore, the receiving hopper is equipped with a vibrator.

[0020] Furthermore, the conveyor belt is provided with two mutually spaced and continuously S-shaped baffles, and the bottom of the receiving hopper is located between the two baffles.

[0021] Therefore, this invention has the following characteristics compared to the prior art: 1. The cleaning equipment can clean the mixture discharged from the reactor multiple times. Combined with a stirrer, it can achieve a better cleaning effect. Furthermore, the mixture of ethylene bis-stearamide and water after cleaning can be directly pumped to the filtration equipment via a discharge pipe using a pumping device; 2. The filtration equipment includes a truss slide rail, a sliding seat, a mounting frame, and a tilting filter frame. The sliding seat can move the tilting filter frame along the truss slide rail to the lower side of the discharge outlet of the discharge pipe and the upper side of the primary drying equipment. The tilting filter frame can efficiently filter out the water in the ethylene bis-stearamide and pour the ethylene bis-stearamide into the primary drying equipment by tilting. Primary drying equipment; 3. The moist ethylene bis-stearamide granules are gradually heated by the drying platform and roughly dried. The tilting table tilts downward to pour out the ethylene bis-stearamide granules; 4. The receiving hopper is used to receive the preliminarily dried ethylene bis-stearamide granules and output them from the discharge gap along the conveyor belt. After being heated by the thermal radiation heating component, they are output from the conveyor belt. The discharge gap can spread the ethylene bis-stearamide granules evenly and evenly on the conveyor belt so that the subsequent thermal radiation heating component can dry them evenly; 5. The receiving hopper is equipped with a vibrator so that the ethylene bis-stearamide granules can fill the lower half of the receiving hopper relatively evenly. Attached Figure Description

[0022] Appendix Figure 1 This is a schematic diagram of the structure of the present invention;

[0023] Appendix Figure 2 This is a structural diagram of the cleaning equipment;

[0024] Appendix Figure 3 This is a top view of the frame;

[0025] Appendix Figure 4 This is a schematic diagram of the primary drying equipment;

[0026] Appendix Figure 5 This is a top view of the tilting table;

[0027] Appendix Figure 6 This is a structural diagram of the paving sheet;

[0028] Appendix Figure 7 This is a diagram showing the positional relationship between the receiving hopper and the conveyor belt;

[0029] Appendix Figure 8 This is a cross-sectional view of the conveyor belt. Detailed Implementation

[0030] The technical solution of the present invention will be further described in detail below through embodiments and in conjunction with the accompanying drawings.

[0031] In the description of this invention, 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," and "counterclockwise," etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings. They are only for the convenience of describing this invention and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, they should not be construed as limitations on this invention.

[0032] Example 1: See Figure 1 A refining production line and process for ethylene bis-stearamide, comprising a cleaning device 100, which includes a cleaning tank 110 and a mixer 120. The bottom of the cleaning tank is provided with a discharge port 13 (see [link to relevant documentation]). Figure 2 );

[0033] Filtration equipment 200;

[0034] Primary drying equipment 300 includes a tilting table 310, a drying platform 320 located on the tilting table, and an electric heating element 330 located inside the tilting table (see...). Figure 4 );

[0035] The secondary drying equipment 400 includes a receiving hopper 410, a conveyor belt 420 located below the receiving hopper, and a thermal radiation heating component 430 located on the path of the conveyor belt. The bottom of the receiving hopper is in contact with the upper surface of the conveyor belt, and a discharge notch 411 is provided on the bottom of the receiving hopper on the side away from the conveyor belt (see [reference]). Figure 7 );

[0036] The production process includes:

[0037] S1. Pour all the mixture after the chemical reaction in the reactor into the cleaning tank, add clean water into the cleaning tank and control the stirrer to rotate and stir. After stirring for a period of time, stop the stirrer and let it stand for a period of time. After draining the upper wastewater, add clean water again and repeat the above steps three times. Finally, a clean mixture of ethylene bis-stearamide and water is obtained. Turn on the stirrer again and open the discharge port to discharge the ethylene bis-stearamide fluid.

[0038] S2 guides the ethylene bis-stearamide fluid discharged from S1 to the filtration equipment for filtration, and removes excess water;

[0039] S3, pour the wet ethylene bis-stearamide granules obtained in S2 onto the drying platform of the primary drying equipment, heat the drying platform with the electric heating element, and after the predetermined time is reached, the tilting table is tilted downward to pour out the ethylene bis-stearamide granules on it.

[0040] S4. Pour the ethylene bis-stearamide granules obtained in S3 into the receiving hopper. The ethylene bis-stearamide granules in the receiving hopper are output from the discharge gap along the conveyor belt, heated by the thermal radiation heating component, and then output from the conveyor belt.

[0041] This embodiment reduces the manpower and material resources spent on loading and unloading materials by redesigning the structure of some production equipment and optimizing the layout, connecting various production equipment in series.

[0042] See Figure 2 A solenoid valve is installed at the discharge port, and a discharge pipe 140 is connected between the discharge port and the filter equipment. A pumping device 150 is installed on the discharge pipe.

[0043] See Figure 2 The upper side of the cleaning tank is equipped with a feed inlet 160, a water inlet 170 and a motor. The motor is connected to the agitator. The bottom of the cleaning tank is also equipped with an upward-extending drain pipe 180.

[0044] See Figure 1 The filtration device includes a truss slide rail 210, a waste liquid collection tank 220, a sliding seat 230 slidably connected to the truss, a mounting frame 240 fixed to the sliding seat, and a flip filter frame 250 rotatably connected to the mounting frame. The sliding seat can move the flip filter frame along the truss slide rail to the lower side of the discharge port of the discharge pipe and the upper side of the primary drying equipment.

[0045] See Figure 1 and Figure 3 The flip filter frame includes a frame 251 and a filter layer 252 laid flat at the bottom of the frame.

[0046] See Figure 5 and Figure 6 The turning table is also equipped with two lead screws 340 and a motor that drives the lead screws to rotate. A material spreader 350 is mounted on both lead screws and rotates simultaneously. The material spreader has two spreading plates 360, and the bottom of the spreading plates is serrated. The motor drives the lead screws to rotate so that the material spreader can move back and forth to achieve reciprocating translation. The spreading plates can push the material on the drying platform back and forth to make it spread evenly.

[0047] See Figure 4 The primary drying equipment also includes a base 380 and a hydraulic cylinder 370 rotatably connected to the base. The tilting table is rotatably connected to the base, and the telescopic rod of the hydraulic cylinder is rotatably connected to the bottom of the tilting table.

[0048] See Figure 7The receiving hopper is equipped with a vibrator 412.

[0049] See Figure 8 The conveyor belt is equipped with two mutually spaced and continuously S-shaped baffles 421, and the bottom of the receiving hopper is located between the two baffles.

[0050] It will be apparent to those skilled in the art that the present invention can be modified in various ways, and such modifications are not considered to depart from the scope of the invention. All such modifications that are obvious to those skilled in the art are included within the scope of the claims.

Claims

1. A refining process for ethylene bis-stearamide, characterized in that: The cleaning equipment includes a cleaning tank and a mixer, and the bottom of the cleaning tank is provided with a discharge port. The cleaning equipment also includes a filtration device; The cleaning equipment also includes a primary drying device, which includes a tilting table, a drying platform located on the tilting table, and an electric heating component located inside the tilting table. The primary drying device also includes a base and a hydraulic cylinder rotatably connected to the base. The tilting table is rotatably connected to the base, and the telescopic rod of the hydraulic cylinder is rotatably connected to the bottom of the tilting table. The tilting table is also provided with two lead screws and a motor that drives the lead screws to rotate. A material spreader is rotatably mounted on both lead screws. The material spreader is provided with two material spreading plates, and the bottom of the material spreading plates is serrated. The cleaning equipment also includes a secondary drying device, which includes a receiving hopper, a conveyor belt located below the receiving hopper, and a thermal radiation heating component located on the path of the conveyor belt. The bottom of the receiving hopper is in contact with the upper surface of the conveyor belt, and a discharge notch is provided on the bottom of the receiving hopper on the side away from the conveyor belt. The production process includes: S1. Pour all the mixture after the chemical reaction in the reactor into the cleaning tank, add clean water into the cleaning tank and control the stirrer to rotate and stir. After stirring for a period of time, stop the stirrer and let it stand for a period of time. After draining the upper wastewater, add clean water again and repeat the above steps at least twice. Finally, obtain a cleaned mixture of ethylene bis-stearamide and water. Turn on the stirrer again and open the discharge port to discharge the ethylene bis-stearamide fluid. S2 guides the ethylene bis-stearamide fluid discharged from S1 to the filtration equipment for filtration, and removes excess water; S3, pour the wet ethylene bis-stearamide granules obtained in S2 into the drying platform of the primary drying equipment, heat the drying platform through the electric heating component, and drive the screw to rotate the motor to realize the reciprocating translation of the spreader. The spreader can push the material on the drying platform back and forth to make it evenly spread. After the predetermined time is reached, the tilting table tilts down to pour out the ethylene bis-stearamide granules on it. S4. Pour the ethylene bis-stearamide granules obtained in S3 into the receiving hopper. The ethylene bis-stearamide granules in the receiving hopper are output from the discharge gap along the conveyor belt, heated by the thermal radiation heating component, and then output from the conveyor belt.

2. The refining process for ethylene bis-stearamide according to claim 1, characterized in that: A solenoid valve is provided at the discharge port, and a discharge pipe is connected between the discharge port and the filter equipment. A pumping device is provided on the discharge pipe.

3. The refining process for ethylene bis-stearamide according to claim 2, characterized in that: The upper side of the cleaning tank is equipped with a feed inlet, a water inlet and a motor. The motor is connected to the agitator. The bottom of the cleaning tank is also equipped with an upward-extending drain pipe.

4. The refining process for ethylene bis-stearamide according to claim 3, characterized in that: The filtration device includes a truss slide rail, a sliding seat slidably connected to the truss, a mounting frame fixed to the sliding seat, and a flip filter frame rotatably connected to the mounting frame. The sliding seat can move the flip filter frame along the truss slide rail to the lower side of the discharge port of the discharge pipe and the upper side of the primary drying device.

5. The refining process for ethylene bis-stearamide according to claim 4, characterized in that: The flip filter frame includes a frame and a filter layer laid flat at the bottom of the frame.

6. The refining process for ethylene bis-stearamide according to claim 1, characterized in that: The receiving hopper is equipped with a vibrator.

7. The refining process for ethylene bis-stearamide according to claim 1, characterized in that: The conveyor belt is provided with two mutually spaced and continuously distributed S-shaped baffles, and the bottom of the receiving hopper is located between the two baffles.

Citation Information

Patent Citations

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