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Terpolymer used for hard polyvinyl chloride and preparation method thereof

A technology of rigid polyvinyl chloride and terpolymer, applied in the field of rigid polyvinyl chloride terpolymer and its preparation, can solve the problems of lowering product price, deviating from overall planning, slow melt plasticization, etc. Achieve reasonable process, improve melt strength and balance torque, and simple steps

Active Publication Date: 2015-02-04
SHANDONG SHITUO HIGH MOLECULAR WEIGHT MATERIAL
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Methyl methacrylate-butyl acrylate (or ethyl acrylate) copolymer has the advantages of excellent processing performance, heat resistance, wide processing temperature range, high melt strength, good surface Smoothness and dimensional stability; compared with acrylate processing modifiers, styrene-acrylonitrile processing modifiers have obvious cost advantages, but because styrene contains unsaturated double bonds, the anti-ultraviolet and anti-aging properties Generally, at the same time, the compatibility of styrene and PVC is relatively poor, the processing range is narrow, the melt plasticization is slow, and the surface finish of the product is not good; the blended resin mixed with nano-modified inorganic fillers is modified by the above two types of processing Based on the agent, it is combined with fillers such as nano-calcium carbonate, silicon dioxide, mica powder, etc., so as to reduce the product price
The greater the amount added, the more obvious the decline in mechanical properties of rigid PVC products, such as increased brittleness of products, slow melt plasticization during processing, decreased surface finish, and dimensional stability that cannot meet expected indicators, etc.
[0004] The present inventor found in the process of researching the technical route and market application of PVC processing modifiers that alkyl methacrylates, alkyl acrylates resins, acrylonitrile, and styrene resins are effective in improving the compatibility of processing aids and PVC. And plasticization has certain advantages, but with the rising price of petrochemical raw materials, the production and application of PVC processing modifiers have to add a large amount of inorganic fillers to reduce costs and seek business development
Eventually, a vicious circle was formed, which seriously hindered the overall level of the rigid PVC products industry and deviated from the national overall plan of "replacing steel with plastic and wood with plastic".

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] (1) Add 225kg of vinyl acetate monomer, 3750kg of deionized water, 0.15kg of polyvinyl alcohol 1788, 0.11kg of sodium lauryl sulfate, and 7.5kg of sodium carbonate medium into the reaction device, ventilate nitrogen and exhaust oxygen, at 50r / min Stir at the stirring speed for 30min, raise the temperature to 45°C, add 0.03kg of potassium persulfate, control the temperature at 55°C for 1h, and use the semi-continuous emulsion polymerization method to prepare the remaining 1225kg of vinyl acetate monomer and 0.64kg of sodium lauryl sulfate , 0.12kg of potassium persulfate was divided into 3 times to initiate polymerization, and reacted at 55°C for 2 hours to prepare the core layer emulsion;

[0031] (2) 7.5kg sodium lauryl sulfate, 1200kg methyl methacrylate, 75kg butyl acrylate are added successively in the nuclear layer emulsion that step (1) obtains, nitrogen exhaust oxygen, under the stirring velocity of 50r / min Stir for 30 minutes, heat up to 40°C, add 0.15 kg of pot...

Embodiment 2

[0035] (1) Add 300kg of vinyl acetate monomer, 4125kg of deionized water, 0.75kg of polyvinyl alcohol 1799, 3kg of sodium dodecylbenzene sulfonate, and 18kg of potassium hydroxide into the reaction device, and ventilate nitrogen to exhaust oxygen. Stir at a stirring speed of min for 30min, heat up to 50°C, add 0.09kg of ammonium persulfate, react at 58°C for 1h, and use semi-continuous emulsion polymerization to prepare the remaining 1200kg of vinyl acetate monomer, 12kg of sodium dodecylbenzenesulfonate, 0.36kg of ammonium persulfate was divided into 3 times to initiate polymerization, and reacted at 58°C for 2 hours to prepare the core layer emulsion;

[0036] (2) 30kg sodium dodecylbenzenesulfonate, 1350kg methyl methacrylate, and 150kg butyl acrylate are added to the nuclear layer emulsion obtained in step (1) successively, nitrogen exhaust oxygen, at a stirring speed of 150r / min Stir at low temperature for 30 minutes, heat up to 50°C, add 0.45 kg of potassium persulfate, ...

Embodiment 3

[0040](1) Add 375kg of vinyl acetate monomer, 4500kg of deionized water, 1.5kg of polyvinyl alcohol 1788, 7.5kg of OP-10, and 30kg of sodium phosphate medium into the reaction device, pass nitrogen to exhaust oxygen, and stir at 300r / min Stir for 30min, heat up to 55°C, add 0.19kg of potassium persulfate, react at 60°C for 1h, use semi-continuous emulsion polymerization to mix the remaining 1125kg of vinyl acetate monomer, 22.5kg of sodium lauryl sulfate, and 0.56kg of sodium bicarbonate Initiate polymerization in 3 times, and react at 60°C for 2 hours to prepare the core layer emulsion;

[0041] (2) Add 45kg sodium lauryl sulfate, 1425kg methyl methacrylate, and 300kg butyl acrylate into the nuclear layer emulsion obtained in step (1) successively, nitrogen exhaust oxygen, and stir at a stirring speed of 300r / min After 30 minutes, the temperature was raised to 45°C, 0.75 kg of potassium persulfate was added, and the reaction temperature was controlled at 52°C for 2.5 hours; ...

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PUM

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Abstract

The invention belongs to the processing auxiliary agent field used for hard polyvinyl chloride, and concretely relates to a terpolymer used for hard polyvinyl chloride and a preparation method thereof. The terpolymer is characterized in that a core layer and a shell layer with mass ratio of 3: 1-4: 1 are prepared by employing a grafting emulsion polymerisation technology, wherein the core layer is prepared by a vinyl acetate monomer, deionized water, a dispersant, an emulsifier, an alkalescence medium and an initiator; and the shell layer is prepared by methyl methacrylate, butyl acrylate monomer, the emulsifier and the initiator. According to the invention, yield is high as more than 98%, the emulsion stability is good, melt-strength and balance torque are greatly increased, water resistance, alkali resistance and heat resistance of the copolymer are increased, production cost is greatly reduced, and cost performance can be increased. The invention also provides a preparation method which has the advantages of simple process and simple operation.

Description

technical field [0001] The invention belongs to the field of processing aids for rigid polyvinyl chloride, and in particular relates to a terpolymer for rigid polyvinyl chloride and a preparation method thereof. Background technique [0002] my country is the world's largest producer and consumer of rigid polyvinyl chloride PVC, and related PVC products have a broad market environment, both powerful and broad. Based on the rapid development of urban and rural construction engineering, transportation engineering, environmental engineering, energy and water conservancy engineering, etc., the market demand for PVC building materials and engineering materials is increasing day by day, and it is currently one of the plastic varieties with the largest output in my country. Rigid PVC does not contain softeners, so it is easy to form, not brittle, non-toxic and pollution-free, and has a long storage time. Great development and application value. [0003] During processing, PVC nee...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F263/04C08F220/14C08F220/18C08F2/26C08F2/30C08L27/06C08L51/00
Inventor 呼建强刘清祥徐茂增孙蒙侯田圣
Owner SHANDONG SHITUO HIGH MOLECULAR WEIGHT MATERIAL
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