CN103665559A - PP pen container special material - Google Patents

PP pen container special material Download PDF

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Publication number
CN103665559A
CN103665559A CN201310658754.1A CN201310658754A CN103665559A CN 103665559 A CN103665559 A CN 103665559A CN 201310658754 A CN201310658754 A CN 201310658754A CN 103665559 A CN103665559 A CN 103665559A
Authority
CN
China
Prior art keywords
pen container
pipe compound
masterbatch
pen
preparation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201310658754.1A
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Chinese (zh)
Inventor
李文
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
QINGDAO DADU NEW MATERIAL SCIENCE & TECHNOLOGY Co Ltd
Original Assignee
QINGDAO DADU NEW MATERIAL SCIENCE & TECHNOLOGY Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by QINGDAO DADU NEW MATERIAL SCIENCE & TECHNOLOGY Co Ltd filed Critical QINGDAO DADU NEW MATERIAL SCIENCE & TECHNOLOGY Co Ltd
Priority to CN201310658754.1A priority Critical patent/CN103665559A/en
Publication of CN103665559A publication Critical patent/CN103665559A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/10Homopolymers or copolymers of propene
    • C08L23/12Polypropene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/02Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
    • C08L2205/025Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)

Abstract

The invention belongs to the field of polymer materials, and specifically relates to a PP pen container special material. The material is composed of the following components in percentage by weight: 60% to 80% of PP with a high melting point, 5% to 20% of PP recycled material, 10% to 15% of flexibilizer, 2% to 3% of flow modifier, and 0.1% to 2% of color master batch. The preparation method comprises steps of mixing, extruding, and injection moulding. The preparation method reasonably utilizes PP recycled material so as to make the product performance meet the requirements of pen container manufacturing, moreover, has the characteristic of saving cost, and can be dedicatedly used to manufacture pen containers.

Description

PP pen container PP Pipe Compound
Technical field
The invention belongs to polymeric material field, be specifically related to a kind of PP pen container PP Pipe Compound.
Background technology
Pen container is seen everywhere in people's study and work, than he can the invention history of existing several thousand, so far people still be unable to do without him, the pen container of various materials, various patterns emerges in an endless stream, it does not still take in the stationery of pen in a kind of study and work, but also often as a kind of Presents Giving relatives and friends of elegance.Along with present material technology is to environmental protection and lightweight development, the plastics of take are made the weight that pen container not only can alleviate pen container as raw material, and due to plastics recoverable, thereby have reduced the consumption of resource.
Polypropylene (PP) is a kind of wide plastics of originating.Its degree of crystallinity is high, compound with regular structure, thereby there is good mechanical property.The absolute value of Mechanical Properties of PP is higher than polyethylene, but in plastic material, still belongs to kind on the low side, and its tensile strength only can reach 30 MPa or slightly high level.The polypropylene that isotactic index is larger has higher tensile strength, but with the raising of isotactic index, the shock strength of material declines to some extent, but no longer changes after dropping to a certain numerical value.Because above-mentioned performance PP is of many uses, especially, in automotive plastic, the consumption of PP is maximum, and rate of growth is the fastest, and it has become the main raw material of collision bumper.
Automotive plastic is as higher mobility, rigidity, toughness and the thermotolerance etc. of collision bumper needs, also to there be good dimensional stability and ageing resistance, but for making pen container, it,, to the mobility of PP, rigidity, toughness, thermotolerance, dimensional stability and the performance such as anti-aging, requires not strict.So PP plastics of the prior art are when when making pen container, its cost is higher, can not meet the requirement of pen container producer to PP material cost.
In prior art; in the producing and selling of PP goods and use procedure, produce a large amount of PP feed backs; as the PP scrap stock that produce in producing the process of automobile windsheild, the PP waste material producing after bumper is discarded, these PP feed backs bring huge pressure to environment protection.
Summary of the invention
For addressing the above problem, the object of the present invention is to provide a kind of PP pen container PP Pipe Compound, it makes product performance reach the making requirement of pen container, and has cost-saving feature by rationally utilizing PP feed back, can be specifically designed to making pen container.
Technical scheme of the present invention is: a kind of PP pen container PP Pipe Compound, and its component by following mass percent forms:
The high molten PP 60%-80% that refers to
PP feed back 5%-20%
Toughner 10%-15%
Flow ability modifying agent 2%-3%
Masterbatch 0.1%-2%.
Optimize, described toughner adopts polyolefin elastomer.
Optimize, described flow ability modifying agent 4,4 '-dihydroxy diphenylsulphone is or/and HP.
Optimize, described Masterbatch adopts black masterbatch.
The preparation method of above-mentioned PP pen container PP Pipe Compound provided by the invention, first it comprise the steps: each component according to mass percent homogenizer stirring and evenly mixing, then proceed in twin screw extruder and melt extrude, cooling, last injection moulding makes product.
Beneficial effect of the present invention is:
1, by rationally utilizing PP feed back, and add toughner and flow ability modifying agent, make the cost of product decline 10%, and physicals all reaches requirement, therefore the product performance that the present invention makes reach the making requirement of pen container, and have cost-saving feature, can be specifically designed to making pen container.
2, by the development to PP pen container PP Pipe Compound, reduced pen container producer's manufacturing cost.
3, by reclaiming PP feed back recycling, be conducive to reduce the wasting of resources, there is the effect of protection of the environment.
Embodiment
Below in conjunction with embodiment, further illustrate the present invention.
The technical scheme of present embodiment is: a kind of PP pen container PP Pipe Compound, and its component by following mass percent forms:
The high molten PP 60%-80% that refers to
PP feed back 5%-20%
Toughner 10%-15%
Flow ability modifying agent 2%-3%
Masterbatch 0.1%-2%.
Wherein, described toughner adopts polyolefin elastomer.
Wherein, described flow ability modifying agent 4,4 '-dihydroxy diphenylsulphone is or/and HP.
Wherein, described Masterbatch adopts black masterbatch.
The preparation method of the above-mentioned PP pen container PP Pipe Compound that present embodiment provides, first it comprise the steps: each component according to mass percent homogenizer stirring and evenly mixing, then proceed in twin screw extruder and melt extrude, cooling, last injection moulding makes product.
Wherein, raw material stirs 5-10min in homogenizer.
Wherein, while extruding, the barrel temperature of twin screw extruder is: back segment 200-210 ℃, stage casing 210-220 ℃, leading portion 220-225 ℃, head temperature 225-230 ℃.
For further illustrating the present invention, present embodiment provides three samples, is designated as sample 1-3, and concrete component, mass percent be in Table 1, and the sample that three embodiment are provided carried out performance test, by outcome record in table 2.
Table 1
Raw material Sample 1 Sample 2 Sample 3
The high molten PP that refers to 60% 70% 80%
PP feed back 20% 15% 5%
Toughner 15% 10% 10%
HP 3% 3% 3%
Black agglomerate 2% 2% 2%
Table 2
Performance Sample 1 Sample 2 Sample 3
Melting index (g/10min) 34 35 37
Shock strength (KJ/m 2 6 6.4 7
Tensile strength (MPa) 20 22 25
Elongation at break 44% 50% 53%
Flexural strength (MPa) 30 33 35
Modulus in flexure (MPa) 1150 1200 1230
Known by upper table, the mobility of the sample that present embodiment provides, rigidity, toughness and intensity all can reach the service requirements of pen container; And the cost of sample, by original 13.5-14.5 unit, can be controlled in below 12.5 yuan, has declined more than 10%.
In sum, the feature of present embodiment is:
1, by rationally utilizing PP feed back, and add toughner and flow ability modifying agent, make the cost of product decline 10%, and physicals all reaches requirement, therefore the product performance that present embodiment makes reach the making requirement of pen container, and there is cost-saving feature, can be specifically designed to making pen container.
2, by the development to PP pen container PP Pipe Compound, reduced pen container producer's manufacturing cost.
3, by reclaiming PP feed back recycling, be conducive to reduce the wasting of resources, there is the effect of protection of the environment.

Claims (4)

1. a PP pen container PP Pipe Compound, is characterized in that: its component by following mass percent forms:
The high molten PP 60%-80% that refers to
PP feed back 5%-20%
Toughner 10%-15%
Flow ability modifying agent 2%-3%
Masterbatch 0.1%-2%.
2. PP pen container PP Pipe Compound according to claim 1, is characterized in that: described toughner adopts polyolefin elastomer.
3. PP pen container PP Pipe Compound according to claim 2, is characterized in that: described flow ability modifying agent 4,4 '-dihydroxy diphenylsulphone is or/and HP.
4. PP pen container PP Pipe Compound according to claim 3, is characterized in that: described Masterbatch adopts black masterbatch.
CN201310658754.1A 2013-12-09 2013-12-09 PP pen container special material Pending CN103665559A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310658754.1A CN103665559A (en) 2013-12-09 2013-12-09 PP pen container special material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310658754.1A CN103665559A (en) 2013-12-09 2013-12-09 PP pen container special material

Publications (1)

Publication Number Publication Date
CN103665559A true CN103665559A (en) 2014-03-26

Family

ID=50304392

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310658754.1A Pending CN103665559A (en) 2013-12-09 2013-12-09 PP pen container special material

Country Status (1)

Country Link
CN (1) CN103665559A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112409682A (en) * 2020-10-09 2021-02-26 扬州龙彩塑料色母粒有限公司 Toughened polypropylene color master batch and preparation method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112409682A (en) * 2020-10-09 2021-02-26 扬州龙彩塑料色母粒有限公司 Toughened polypropylene color master batch and preparation method thereof

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WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20140326

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