IP Library Granted Patent US 12668694
Granted Patent B2
US 12668694 · App. 18/274,467 · Granted Jun 30, 2026

Recycled Material Based on in-situ compatibilization and chain extension and preparation method therefor

Inventors: Yonggao Fu (Guangdong, CN); Nuo Cao (Guangdong, CN); Jiaqi Hu (Guangdong, CN); Ling Wang (Guangdong, CN); Chao Wan (Guangdong, CN)
Assignee: CHINA NATIONAL ELECTRIC APPARATUS RESEARCH INSTITUTE CO., LTD.
C08L25/06C08L23/12B29B7/007B29B7/484B29B7/72B29B9/06B29K2023/12B29K2025/06B29K2105/0014B29K2105/26B29K2995/0077B29K2995/0089C08L2205/025C08L2205/035C08L2205/08C08L2205/14C08L2207/20C08L2312/00
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Quick Facts
Patent No.
US 12668694
App. No.
18/274,467
Granted
Jun 30, 2026
Kind
B2
Abstract

A recycled material based on in-situ compatibilization and chain extension is mainly prepared from the following raw materials in parts by mass: 30-70 parts of waste HIPS, 30-70 parts of waste PP, 2-6 parts of POE, 0.1-0.4 part of an alkylation reaction catalyst, 0.1-0.3 part of a co-catalyst, and 2-8 parts of a macromolecular chain extender. Further, a preparation method for the recycled material based on in-situ compatibilization and chain extension is provided.

Claims (22)

1 . A recycled material based on in-situ compatibilization and chain extension, wherein the recycled material is mainly prepared from the following raw materials in parts by mass:

30-70 parts of waste high-impact polystyrene;

30-70 parts of waste polypropylene;

2-6 parts of polyolefin elastomer;

0.1-0.4 part of an alkylation reaction catalyst;

0.1-0.3 part of a co-catalyst; and

2-8 parts of a macromolecular chain extender.

2 . The recycled material based on in-situ compatibilization and chain extension according to claim 1 , wherein the waste high-impact polystyrene is a flaky material obtained from waste high impact polystyrene which is crushed and homogenized.

3 . The recycled material based on in-situ compatibilization and chain extension according to claim 1 , wherein the waste polypropylene is a flaky material obtained from waste polypropylene which is crushed and homogenized.

4 . The recycled material based on in-situ compatibilization and chain extension according to claim 1 , wherein the polyolefin elastomer is a novel ethylene-octene copolymer elastomer material.

5 . The recycled material based on in-situ compatibilization and chain extension according to claim 1 , wherein the alkylation reaction catalyst is anhydrous aluminum chloride.

6 . The recycled material based on in-situ compatibilization and chain extension according to claim 1 , wherein the co-catalyst is styrene.

7 . The recycled material based on in-situ compatibilization and chain extension according to claim 1 , wherein the macromolecular chain extender is a high-impact polystyrene grafted glycidyl methacrylate.

8 . A preparation method for the recycled material based on in-situ compatibilization and chain extension according to claim 1 , comprising the following steps:

mixing the waste high-impact polystyrene in 30-70 parts, the waste polypropylene in 30-70 parts, the polyolefin elastomer in 2-6 parts, the alkylation reaction catalyst in 0.1-0.4 part, and the co-catalyst in 0.1-0.03 part to obtain a mixed material;

adding the mixed material from a main feeding device of a twin screw extruder and melting the mixed material;

controlling a screw speed to 40 to 80 rpm;

adding the macromolecular chain extender in 2-8 parts to a fifth zone of a processing middle section of the twin screw extruder;

blending with the molten mixed material; and

extruding, drawing, cooling and pelletizing to obtain the recycled material based on in-situ compatibilization and chain extension.

9 . The preparation method for the recycled material based on in-situ compatibilization and chain extension according to claim 8 , wherein a processing temperature zone of the twin screw extruder is 175 to 235° C.

10 . The preparation method for the recycled material based on in-situ compatibilization and chain extension according to claim 8 , wherein temperatures of eight processing zones of the twin screw extruder are: 180° C., 180° C., 185° C., 185° C., 235° C., 235° C., 230° C., and 230° C. in sequence.