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Manufacturing method for polyolefin fiber for adsorbing organic liquid

A polyolefin fiber and organic liquid technology, applied in the field of fiber modification, can solve problems such as complex preparation process, poor fiber formation, and limited scale application, and achieve excellent comprehensive performance, wide applicability, and good mechanical properties

Inactive Publication Date: 2012-03-21
TIANJIN POLYTECHNIC UNIV +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This type of fiber has the characteristics of good oil-water selectivity and large adsorption capacity. However, due to the inherent characteristics of the copolymer itself, the fiber formation during spinning is poor, plasticizers are required for plasticization, and the preparation process is complicated. The performance is poor, and the textile processing performance is not ideal, and the industrial scale application is limited

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] In the polymerization kettle, add polymer monomers with a volume of 1600ml and 7.5g of initiator benzoyl peroxide, 24g of dispersant polyvinyl alcohol and 4800ml of deionized water, stir well to a homogeneous solution, and then pass into nitrogen to carry out Protect, raise the temperature to 85°C, react for 5 hours, increase the reaction temperature to 95°C, continue the reaction for 1 hour, terminate the reaction, take out the product, wash, dry, and pulverize to obtain a white powdery copolymer. Wherein, the polymer monomers are n-butyl methacrylate and hydroxyethyl methacrylate, and the mass ratio of the two is 95:5.

[0023] After the obtained copolymer is fully dried, it is mixed with polypropylene pellets (PP H-T03) according to a mass ratio of 1:1, and pelletized in a twin-screw extruder, and the temperature in different regions of the screw is controlled at 195-210°C; The extruded strip blend is further mixed uniformly by cutting or pulverizing to obtain a pell...

Embodiment 2

[0026] In the polymerization kettle, add polymer monomers with a volume of 1600ml and 7.5g of initiator benzoyl peroxide, 24g of dispersant polyvinyl alcohol and 4800ml of deionized water, stir well to a homogeneous solution, and then pass into nitrogen to carry out Protect, raise the temperature to 85°C, react for 5 hours, increase the reaction temperature to 95°C, continue the reaction for 1 hour, terminate the reaction, take out the product, wash, dry, and pulverize to obtain a white powdery copolymer. Wherein, the polymer monomers are n-butyl methacrylate and hydroxyethyl methacrylate with a mass ratio of 95:5.

[0027] After the obtained copolymer is fully dried, it is mixed with polypropylene pellets (PP H-T03) according to the mass ratio of 3:7, and pelletized in a twin-screw extruder. between. The extruded strip blend is further mixed uniformly by cutting or pulverizing to obtain a pellet or powder blend;

[0028] Feed the obtained pellets or powder into a twin-screw...

Embodiment 3

[0030] In the polymerization kettle, add polymer monomers with a volume of 1600ml and 7.5g of initiator benzoyl peroxide, 24g of dispersant polyvinyl alcohol and 4800ml of deionized water, stir well to a homogeneous solution, and then pass into nitrogen to carry out Protect, raise the temperature to 85°C, react for 5 hours, increase the reaction temperature to 95°C, continue the reaction for 1 hour, terminate the reaction, take out the product, wash, dry, and pulverize to obtain a white powdery copolymer. Wherein, the polymer monomers are n-butyl methacrylate and hydroxyethyl methacrylate with a mass ratio of 95:5.

[0031] After the obtained copolymer is fully dried, it is mixed with high-density polyethylene pellets at a mass ratio of 7:3, and pelletized in a twin-screw extruder, and the temperature in different regions of the screw is controlled between 185 and 200°C. The extruded strip blend is further mixed uniformly by cutting or pulverizing to obtain a pellet or powder ...

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PUM

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Abstract

The invention discloses a manufacturing method for a polyolefin fiber for adsorbing an organic liquid, which comprises the following steps: 1) adding 500-2000ml polymeric monomers, initiating agents accounting for 0.5-0.8% of the total mass of the polymeric monomers, 1500-6000ml deionized water and dispersing agents accounting for 0.5-1% of the total mass of the deionized water into a polymeric kettle, fully stirring till forming a homogeneous phase solution, and then introducing nitrogen, heating up to 80-85 DEG C and reacting for 2-5 hours, and then heating up to 90-95 DEG C and continuing reacting for 1-2 hours, thereby obtaining a reaction product; washing, drying and crushing the reaction product, thereby obtaining a white powdered copolymer; 2) drying the obtained copolymer, mixing the copolymer with polyolefin granular materials according to the mass fraction of (10-50):(90-50), and then extruding from a double-screw machine and pelletizing, wherein the polyolefin granular materials are fibrous polypropylene or polyethylene granular materials with a spinning temperature of 140-250 DEG C; and 3) melting and spinning the granular materials by using the double-screw machine, thereby obtaining the polyolefin fiber.

Description

technical field [0001] The invention relates to fiber modification technology, in particular to a method for manufacturing polyolefin fibers that absorb organic liquids, in particular to a modified polyolefin blended with methacrylate polymers that can absorb organic liquids and polypropylene or polyethylene Fiber manufacturing method. Background technique [0002] At present, the water body environmental pollution caused by the frequent leakage of industrial waste liquids and offshore oil tankers and oil wells is becoming more and more serious, which has posed a serious threat to aquatic organisms and human health. Adsorption treatment of oil spills is considered to be the most potential and feasible treatment method. Oil-absorbing resin is a new type of functional polymer material, which has the advantages of high absorption rate, good oil-water selectivity, and good oil retention under pressure. In 1966, American Dow Chemical Company developed an oil-absorbing resin (JP...

Claims

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Application Information

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IPC IPC(8): D01F6/52D01F6/46B01J20/26B01J20/28B01J20/30D01D5/08D01D1/00
Inventor 肖长发赵健徐乃库封严程博闻杨竹强
Owner TIANJIN POLYTECHNIC UNIV
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