CN108017828A - A kind of preparation method of plastics deicer - Google Patents

A kind of preparation method of plastics deicer Download PDF

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Publication number
CN108017828A
CN108017828A CN201610961628.7A CN201610961628A CN108017828A CN 108017828 A CN108017828 A CN 108017828A CN 201610961628 A CN201610961628 A CN 201610961628A CN 108017828 A CN108017828 A CN 108017828A
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CN
China
Prior art keywords
plastics
deicer
calcium oxide
anhydrous calcium
molecular weight
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
CN201610961628.7A
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Chinese (zh)
Inventor
吴廷禄
曾亚丽
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Chengdu Sheng Technology Co Ltd
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Chengdu Sheng Technology Co Ltd
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Application filed by Chengdu Sheng Technology Co Ltd filed Critical Chengdu Sheng Technology Co Ltd
Priority to CN201610961628.7A priority Critical patent/CN108017828A/en
Publication of CN108017828A publication Critical patent/CN108017828A/en
Pending legal-status Critical Current

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    • 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
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/08Copolymers of ethene
    • C08L23/0846Copolymers of ethene with unsaturated hydrocarbons containing other atoms than carbon or hydrogen atoms
    • C08L23/0853Vinylacetate
    • 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
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/06Polyethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L33/00Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Compositions of derivatives of such polymers
    • C08L33/04Homopolymers or copolymers of esters
    • C08L33/06Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, which oxygen atoms are present only as part of the carboxyl radical
    • C08L33/10Homopolymers or copolymers of methacrylic acid esters
    • C08L33/12Homopolymers or copolymers of methyl methacrylate
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L77/00Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
    • C08L77/06Polyamides derived from polyamines and polycarboxylic acids
    • 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
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2207/00Properties characterising the ingredient of the composition
    • C08L2207/06Properties of polyethylene
    • C08L2207/066LDPE (radical process)

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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)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

The present invention relates to a kind of preparation method of plastics deicer.The plastics deicer main component is anhydrous calcium oxide micro mist, three(Dioctyl pyrophosphoryl epoxide)Isopropyl titanate, ethylene-vinyl acetate copolymer, low molecular weight polyethylene.The preparation method of the plastics deicer is first to crush anhydrous calcium oxide, is prepared into anhydrous calcium oxide micro mist, then is mixed by weight percentage with other constituents, is made through bispin screw pelletizer extruding pelletization.Use, without heating, drying, do not consume energy, water removal effect is splendid after the plastics deicer is directly mixed by 1 3% weight with water containing plastic during use.

Description

A kind of preparation method of plastics deicer
Technical field
The invention belongs to technical field of plastic, is related to a kind of preparation method of plastics deicer.
Background technology
All plastics all contain a certain amount of moisture, need to remove the moisture in plastics, ability in plastics secondary operation Processing(Extrusion, injection, blowing, calendering)Go out the plastic products of qualification.
Common plastics water-eliminating method, is that plastics are added heat drier, the moisture in plastics is allowed by thermal evaporation, so as to remove The moisture in plastics is removed, or is removed the moisture in plastics with the method for heated-air drying.The physics water removal of this heat drying Method, must there is special drying equipment, drying time length(Generally want 2-6 hours), energy consumption is higher, adds plastic processing Cost.And the micro condensation water for being contained in plastic pellet bubble is difficult to remove.
The purpose of the present invention is disclosing a kind of chemical water-eliminating method of plastics, it is to utilize deicer, passes through chemical reaction Mode, absorbs micro-moisture contained in plastics and is combined to novel substance, and removes the moisture in plastics.
The water-eliminating method is that secondary operation is directly carried out after deicer is mixed with plastics, without special drying equipment, Save time and power, easy to use, the plastics water removal suitable for opaque plastic product secondary processing process.
The content of the invention
The present invention is realized by the technical solution of following technical measures composition.
The present invention discloses a kind of preparation method of plastics deicer.The plastics deicer is by anhydrous calcium oxide micro mist three (Dioctyl pyrophosphoryl epoxide)Isopropyl titanate, ethylene-vinyl acetate copolymer and low molecular weight polyethylene, by melting mixing Made of extruding pelletization.The percentage by weight of the deicer each component is:
Anhydrous calcium oxide micro mist 70-83%
Three(Dioctyl pyrophosphoryl epoxide)Isopropyl titanate 1-3%
Ethylene-vinyl acetate copolymer 15-25%
Low molecular weight polyethylene 1-2%
The anhydrous calcium oxide micro mist in the above-mentioned technical solutions, is to smash anhydrous calcium oxide into particle diameter at 100-110 DEG C Micro mist less than 10 microns, the preferred scope of its weight percentage is 70-80%;Three(Dioctyl pyrophosphoryl epoxide)Metatitanic acid is different Propyl ester purity is technical grade, its weight percentage general control is in 1.5-2.5%;Low molecular weight polyethylene molecular weight is less than 3000, its weight percentage general control is in 1.5-2%.
A kind of preparation method of plastics deicer disclosed by the invention:Anhydrous calcium oxide micro mist is added and has warmed up 100- In 110 DEG C of super mixer, three are added(Dioctyl pyrophosphoryl epoxide)Isopropyl titanate, high-speed stirred 2-3 minutes, adds Ethylene-vinyl acetate copolymer, high-speed stirred 2 minutes.Double-screw extruding pelletizing machine is added after releasing, in 120-160 DEG C of temperature Lower melting extrusion is granulated, and the particle that will eventually cause is put into super mixer, is added low molecular weight polyethylene, is stirred at 120 DEG C Mix 1-2 minutes, plastics deicer.
A kind of plastics deicer disclosed by the invention, it is a kind of chemical water-eliminating method, it, which removes water principle, is:
Anhydrous calcium oxide micro mist in deicer, the water run into plastics chemically react, and generation one kind can be filled out as plastics The material calcium hydroxide of charge, so as to eliminate the moisture in plastics, i.e. CaO+H2O→Ca(OH)2.
A kind of plastics deicer disclosed by the invention, application method are to add the deicer of 1-5% in the plastic, are uniformly mixed Afterwards, it is directly used in the melting extrusion processing of plastic products.Deicer can also be mixed with plastics it is even after, first make once grain, then The processing of plastic products is carried out, simple and convenient using the deicer, not power consumption, does not take.Being processed into for plastic products can be reduced This.
Embodiment:
By embodiment, the present invention is further described in detail.In example given below, the percentage of each component is Percentage by weight of the group in deicer constituent.
Embodiment 1
Anhydrous calcium oxide micro mist 75%
Three(Dioctyl pyrophosphoryl epoxide)Isopropyl titanate 1.5%
Ethylene-vinyl acetate copolymer 22%
Low molecular weight polyethylene 1.5%
Super mixer is warming up to 100-110 DEG C in advance, adds anhydrous calcium oxide micro mist, and three(Dioctyl pyrophosphoryl epoxide)Titanium Isopropyl propionate, high-speed stirred 3 minutes, adds ethylene-vinyl acetate copolymer, and high-speed stirred 2 minutes, releases mixture, adds The pre- double-screw plastic granulator for being warming up to 120-160 DEG C, melting extrusion are granulated, and then the particle by caused by is put into mixed at high speed In device, low molecular weight polyethylene is added, in 120 DEG C of high-speed stirreds one minute, that is, plastics deicer is made.
Embodiment 2
Anhydrous calcium oxide micro mist 76%
Three(Dioctyl pyrophosphoryl epoxide)Isopropyl titanate 2%
Ethylene-vinyl acetate copolymer 20%
Low molecular weight polyethylene 2%
Super mixer is warming up to 100-110 DEG C in advance, adds anhydrous calcium oxide micro mist and three(Dioctyl pyrophosphoryl epoxide)Titanium Isopropyl propionate, high-speed stirred 3 minutes, adds ethylene-vinyl acetate copolymer, then high-speed stirred 2 minutes, releases mixture, add Enter the pre- double-screw plastic granulator for being warming up to 120-160 DEG C, melting extrusion is granulated, and then the particle by caused by is put into mixed at a high speed In clutch, low molecular weight polyethylene is added, in 120 DEG C of high-speed stirreds one minute, that is, plastics deicer is made.
Embodiment 3
Anhydrous calcium oxide micro mist 80%
Three(Dioctyl pyrophosphoryl epoxide)Isopropyl titanate 2%
Ethylene-vinyl acetate copolymer 16%
Low molecular weight polyethylene 2%
Super mixer is warming up to 100-110 DEG C in advance, adds anhydrous calcium oxide micro mist and three(Dioctyl pyrophosphoryl epoxide)Titanium Isopropyl propionate, high-speed stirred 3 minutes, adds ethylene-vinyl acetate copolymer, then high-speed stirred 2 minutes, releases mixture, add Enter the pre- double-screw plastic granulator for being warming up to 120-160 DEG C, melting extrusion is granulated, and then the particle by caused by is put into mixed at a high speed In clutch, low molecular weight polyethylene is added, in 120 DEG C of high-speed stirreds one minute, that is, plastics deicer is made.
1 plastics deicer application effect of table compares

Claims (6)

1. a kind of plastics deicer preparation method, it is characterised in that the plastics deicer mainly contains anhydrous calcium oxide micro mist, three (Dioctyl pyrophosphoryl epoxide)Isopropyl titanate, ethylene-vinyl acetate copolymer, low molecular weight polyethylene, the weight hundred of component Point ratio is:
Anhydrous calcium oxide micro mist 70-83%
Three(Dioctyl pyrophosphoryl epoxide)Isopropyl titanate 1-3%
Ethylene-vinyl acetate copolymer 15-25%
Low molecular weight polyethylene 1-2%.
2. plastics deicer according to claim 1, it is characterised in that the anhydrous calcium oxide micro mist, particle diameter are less than 10 Micron.
3. plastics deicer according to claim 1, it is characterised in that described three(Dioctyl pyrophosphoryl epoxide)Metatitanic acid Isopropyl ester, purity are technical grade.
4. plastics deicer according to claim 1, it is characterised in that the ethylene-vinyl acetate copolymer, VA contain Measure as 25-30%;Average molecular weight 2000.
5. plastics deicer according to claim 1, it is characterised in that the low molecular weight polyethylene, molecular weight are less than 3000。
First to crush anhydrous calcium oxide micro mist is made 6. plastics deicer preparation method according to claim 1, then with its He mixes component thing by weight percentage, is made through double-screw plastic granulator extruding pelletization.
CN201610961628.7A 2016-10-28 2016-10-28 A kind of preparation method of plastics deicer Pending CN108017828A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610961628.7A CN108017828A (en) 2016-10-28 2016-10-28 A kind of preparation method of plastics deicer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610961628.7A CN108017828A (en) 2016-10-28 2016-10-28 A kind of preparation method of plastics deicer

Publications (1)

Publication Number Publication Date
CN108017828A true CN108017828A (en) 2018-05-11

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Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020028029A (en) * 2000-10-06 2002-04-15 권문구 Poly vinyl chloride insulator for wire
CN1594410A (en) * 2004-07-06 2005-03-16 黄定强 High performance anti-foaming dehumidification master batch for plastic process
CN1611534A (en) * 2003-10-31 2005-05-04 丁少忠 Dehumidifying agent for plastic shaping and its preparing method
CN1903927A (en) * 2006-07-18 2007-01-31 黄定敏 Plastic moisture removing foam eliminating mother particle
CN102070808A (en) * 2009-11-20 2011-05-25 梁树旺 Dehydrating and drying master batch for plastic pipe and production method thereof
CN102311570A (en) * 2011-08-05 2012-01-11 大连方盛塑料有限公司 Dehumidizer for plastic molding
CN103627060A (en) * 2012-08-21 2014-03-12 上海心尔新材料科技股份有限公司 Long-acting defoaming dehumidifying drying master batch for plastic processing and preparation method thereof
CN104130495A (en) * 2014-08-12 2014-11-05 廊坊华博环保材料有限公司 Water removal master batch for plastic drip irrigation pipe or drip irrigation zone and preparation method of water removal master batch
CN105086068A (en) * 2015-08-20 2015-11-25 福建博大塑业新材料有限公司 Water-absorbing granule for HDPE (high-density polyethylene) tubes, and preparation method and application thereof

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020028029A (en) * 2000-10-06 2002-04-15 권문구 Poly vinyl chloride insulator for wire
CN1611534A (en) * 2003-10-31 2005-05-04 丁少忠 Dehumidifying agent for plastic shaping and its preparing method
CN1594410A (en) * 2004-07-06 2005-03-16 黄定强 High performance anti-foaming dehumidification master batch for plastic process
CN1903927A (en) * 2006-07-18 2007-01-31 黄定敏 Plastic moisture removing foam eliminating mother particle
CN102070808A (en) * 2009-11-20 2011-05-25 梁树旺 Dehydrating and drying master batch for plastic pipe and production method thereof
CN102311570A (en) * 2011-08-05 2012-01-11 大连方盛塑料有限公司 Dehumidizer for plastic molding
CN103627060A (en) * 2012-08-21 2014-03-12 上海心尔新材料科技股份有限公司 Long-acting defoaming dehumidifying drying master batch for plastic processing and preparation method thereof
CN104130495A (en) * 2014-08-12 2014-11-05 廊坊华博环保材料有限公司 Water removal master batch for plastic drip irrigation pipe or drip irrigation zone and preparation method of water removal master batch
CN105086068A (en) * 2015-08-20 2015-11-25 福建博大塑业新材料有限公司 Water-absorbing granule for HDPE (high-density polyethylene) tubes, and preparation method and application thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
谢圣英 主编: "《塑料材料》", 31 January 2010, 中国轻工业出版社 *

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