CN102516631A - Processing modifier for low-pressure polyethylene waste tube material and use method thereof - Google Patents
Processing modifier for low-pressure polyethylene waste tube material and use method thereof Download PDFInfo
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- CN102516631A CN102516631A CN201110412496XA CN201110412496A CN102516631A CN 102516631 A CN102516631 A CN 102516631A CN 201110412496X A CN201110412496X A CN 201110412496XA CN 201110412496 A CN201110412496 A CN 201110412496A CN 102516631 A CN102516631 A CN 102516631A
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- tube material
- pressure polyethylene
- low pressure
- modifier
- useless
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
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- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
The invention discloses a processing modifier for a low-pressure polyethylene waste tube material and a use method thereof. The processing modifier comprises 1.1-2.1 parts by weight of chlorinated polyethylene. The use method of the invention comprises the following steps: 1, processing the low-pressure polyethylene waste tube material; 2, detecting the melt flow index of the low-pressure polyethylene waste tube material; 3, uniformly mixing the low-pressure polyethylene waste tube material and chlorinated polyethylene according to a ratio of 100:1.1-2.1 in a mixer for 10-15min under normal temperature conditions, and shutting down the mixer; and 4, discharging, and packaging. The modifier has the advantages of reasonable technology, simple processing, convenient use, effective improvement of physicochemical performances of the low-pressure polyethylene waste tube material, product quality improvement and the like. The modifier can be widely used for the modification processing of low-pressure polyethylene waste tube materials.
Description
Technical field
The present invention relates to a kind of processing of plastic properties-correcting agent and method of use of being used for, particularly relate to a kind of modifier and method of use thereof that is used for the useless tube material of low pressure polyethylene.
Background technology
As everyone knows, the useless tube material processing means of existing low pressure polyethylene is outmoded, technology falls behind, and the product physical and chemical performance of producing is lower, second-rate, can not satisfy the demands of consumers, and also can not adapt to the demand of market development, thereby limits its range of application.
Summary of the invention
The objective of the invention is in order to overcome the deficiency of above-mentioned background technology concentrating on studies and, a kind of modifier and method of use thereof that is used for the useless tube material of low pressure polyethylene is provided through the contriver through producing actual repeated validation.
To achieve these goals, technical scheme of the present invention is such:
A kind of modifier that is used for the useless tube material of low pressure polyethylene provided by the invention, described modifier comprises following component and weight part thereof: chlorinatedpolyethylene 1.1~2.1.
In technique scheme, described modifier comprises following component and weight part thereof: chlorinatedpolyethylene 1.6.
A kind of method of use that is used for the modifier of the useless tube material of low pressure polyethylene provided by the invention; May further comprise the steps: step 1, the useless tube material water of low pressure polyethylene is cleaned; Remove foreign material and dust; To remove the useless tube material of clean low pressure polyethylene again and cut into the close material of size, subsequent use; The melt flow index of step 2, the useless tube material of detection low pressure polyethylene, setting melt flow index M1 is 0.5~3.0; Step 3, the useless tube material of above-mentioned subsequent use low pressure polyethylene is dropped in the mixing machine; Again in the preparation of following ratio: the low pressure polyethylene tube material that gives up: chlorinatedpolyethylene=100: 1.1~2.1; Mixing drops in the mixing machine, and start is 10~15 minutes under normal temperature condition, shuts down; Step 4, the above-mentioned mixture discharging packing that processes get final product.
In technique scheme, when said melt flow index M1=0.5~0.8, the useless tube material of low pressure polyethylene then: chlorinatedpolyethylene=100: 1.1; When said melt flow index M1=0.8~1.5, the useless tube material of low pressure polyethylene then: chlorinatedpolyethylene=100: 1.4; When said melt flow index M1=1.5~2.0, the useless tube material of low pressure polyethylene then: chlorinatedpolyethylene=100: 1.6; When said melt flow index M1=2.0~3.0, the useless tube material of low pressure polyethylene then: chlorinatedpolyethylene=100: 2.1.
The present invention is alleged is used for the modifier and the method for use thereof of the useless tube material of low pressure polyethylene, has following beneficial effect: novel, technology rationally, processing is simple, easy to use, can realize requirement of industrialized batch production.The present invention can improve the physical and chemical performance of the useless tube material of low pressure polyethylene effectively, reduces melt flow index, makes material increase toughness and intensity, has the PP Pipe Compound of squeezing effective way thereby become.The present invention can be widely used for the modification processing of the useless tube material of low pressure polyethylene.
Embodiment
Below in conjunction with embodiment the present invention is made further detailed description, but this embodiment should not be construed as limitation of the present invention.
Embodiment 1
Modifier of the present invention is prepared by following component and weight part: when melt flow index M1=0.5~0.8 of detecting the useless tube material of low pressure polyethylene, then get chlorinatedpolyethylene 1.1, and subsequent use; Its method of use is following:
The useless tube material water of low pressure polyethylene is cleaned, cuts into the close useless pipe material of size after removing foreign material and dust, get 100 parts subsequent use;
Earlier the useless tube material of above-mentioned 100 parts of low pressure polyethylenes having handled is dropped in the mixing machine, more above-mentioned 1.1 parts of chlorinatedpolyethylenees are dropped in the mixing machine, start is 10 minutes under normal temperature condition, shuts down, and the discharging packing gets final product.
Embodiment 2
Present embodiment and embodiment 1 are basic identical, and difference is: when described melt flow index M1=0.8~1.5, then get 1.4 parts of chlorinatedpolyethylenees.
In the method for use the useless tube material of above-mentioned 100 parts of low pressure polyethylenes having handled is dropped in the mixing machine, more above-mentioned 1.4 parts of chlorinatedpolyethylenees are dropped in the mixing machine, start is 12 minutes under normal temperature condition, shuts down, and the discharging packing gets final product.
Embodiment 3
Present embodiment and embodiment 1 are basic identical, and difference is: when described melt flow index M1=1.5~2.0, then get 1.6 parts of chlorinatedpolyethylenees.
In the method for use the useless tube material of above-mentioned 100 parts of low pressure polyethylenes having handled is dropped in the mixing machine, more above-mentioned 1.6 parts of chlorinatedpolyethylenees are dropped in the mixing machine, start is 14 minutes under normal temperature condition, shuts down, and the discharging packing gets final product.
Embodiment 4
Present embodiment and embodiment 1 are basic identical, and difference is: when described melt flow index M1=2.0~3.0, then get 2.1 parts of chlorinatedpolyethylenees.
In the method for use the useless tube material of above-mentioned 100 parts of low pressure polyethylenes having handled is dropped in the mixing machine, more above-mentioned 2.1 parts of chlorinatedpolyethylenees are dropped in the mixing machine, start is 15 minutes under normal temperature condition, shuts down, and the discharging packing gets final product.
Obviously, those skilled in the art can carry out various changes and modification to the present invention and not break away from the spirit and scope of the present invention.Like this, belong within the scope of claim of the present invention and equivalent technologies thereof if of the present invention these are revised with modification, then the present invention also is intended to comprise these changes and modification interior.
The content of not doing in this specification sheets to describe in detail belongs to this area professional and technical personnel's known prior art.
Claims (4)
1. modifier that is used for the useless tube material of low pressure polyethylene, it is characterized in that: described modifier comprises following component and weight part thereof: chlorinatedpolyethylene 1.1~2.1.
2. the modifier that is used for the useless tube material of low pressure polyethylene according to claim 1, it is characterized in that: described modifier comprises following component and weight part thereof: chlorinatedpolyethylene 1.6.
3. method of use that is used for the modifier of the useless tube material of low pressure polyethylene is characterized in that: may further comprise the steps:
Step 1, the useless tube material water of low pressure polyethylene is cleaned, remove foreign material and dust, will remove the useless tube material of clean low pressure polyethylene again and cut into big or small close material, subsequent use;
The melt flow index of step 2, the useless tube material of detection low pressure polyethylene, setting melt flow index M1 is 0.5~3.0;
Step 3, the useless tube material of above-mentioned subsequent use low pressure polyethylene is dropped in the mixing machine; Again in the preparation of following ratio: the low pressure polyethylene tube material that gives up: chlorinatedpolyethylene=100: 1.1~2.1; Mixing drops in the mixing machine, and start is 10~15 minutes under normal temperature condition, shuts down;
Step 4, the above-mentioned mixture discharging packing that processes get final product.
4. the method for use that is used for the modifier of the useless tube material of low pressure polyethylene according to claim 3 is characterized in that:
When said melt flow index M1=0.5~0.8, the useless tube material of low pressure polyethylene then: chlorinatedpolyethylene=100: 1.1;
When said melt flow index M1=0.8~1.5, the useless tube material of low pressure polyethylene then: chlorinatedpolyethylene=100: 1.4;
When said melt flow index M1=1.5~2.0, the useless tube material of low pressure polyethylene then: chlorinatedpolyethylene=100: 1.6;
When said melt flow index M1=2.0~3.0, the useless tube material of low pressure polyethylene then: chlorinatedpolyethylene=100: 2.1.
Priority Applications (1)
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CN201110412496XA CN102516631A (en) | 2011-12-12 | 2011-12-12 | Processing modifier for low-pressure polyethylene waste tube material and use method thereof |
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CN201110412496XA CN102516631A (en) | 2011-12-12 | 2011-12-12 | Processing modifier for low-pressure polyethylene waste tube material and use method thereof |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103333391A (en) * | 2013-06-20 | 2013-10-02 | 中塑联新材料科技湖北有限公司 | Compatible modifying agent for low-pressure polyethylene waste plate material and application method of compatible modifying agent |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5834535A (en) * | 1995-08-21 | 1998-11-10 | General Motors Corporation | Moldable intumescent polyethylene and chlorinated polyethylene compositions |
CN101628999A (en) * | 2009-08-13 | 2010-01-20 | 湖北众联塑业有限公司 | PE waste plastic modifier and reductive modification method thereof |
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2011
- 2011-12-12 CN CN201110412496XA patent/CN102516631A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5834535A (en) * | 1995-08-21 | 1998-11-10 | General Motors Corporation | Moldable intumescent polyethylene and chlorinated polyethylene compositions |
CN101628999A (en) * | 2009-08-13 | 2010-01-20 | 湖北众联塑业有限公司 | PE waste plastic modifier and reductive modification method thereof |
Non-Patent Citations (1)
Title |
---|
杨金平: "聚乙烯与氯化聚乙烯共混的研究", 《中国塑料》, vol. 13, no. 5, 31 May 1999 (1999-05-31) * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103333391A (en) * | 2013-06-20 | 2013-10-02 | 中塑联新材料科技湖北有限公司 | Compatible modifying agent for low-pressure polyethylene waste plate material and application method of compatible modifying agent |
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Application publication date: 20120627 |