[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

DE2354529A1 - Polyethylene contg. homogeneously distributed additives - by high speed mixing of liquid additives with heated resin - Google Patents

Polyethylene contg. homogeneously distributed additives - by high speed mixing of liquid additives with heated resin

Info

Publication number
DE2354529A1
DE2354529A1 DE19732354529 DE2354529A DE2354529A1 DE 2354529 A1 DE2354529 A1 DE 2354529A1 DE 19732354529 DE19732354529 DE 19732354529 DE 2354529 A DE2354529 A DE 2354529A DE 2354529 A1 DE2354529 A1 DE 2354529A1
Authority
DE
Germany
Prior art keywords
additives
tac
polyethylene
added
degrees
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.)
Withdrawn
Application number
DE19732354529
Other languages
German (de)
Inventor
Frank Heil
Fred Dipl Chem Dr Rer Schimke
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.)
OBERSPREE KABELWERKE VEB K
Original Assignee
OBERSPREE KABELWERKE VEB K
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 OBERSPREE KABELWERKE VEB K filed Critical OBERSPREE KABELWERKE VEB K
Publication of DE2354529A1 publication Critical patent/DE2354529A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/20Compounding polymers with additives, e.g. colouring
    • C08J3/203Solid polymers with solid and/or liquid additives
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/04Homopolymers or copolymers of ethene
    • C08J2323/06Polyethene
    • 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
    • C08L2312/00Crosslinking

Landscapes

  • 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)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

Prodn. of polyethylene contg. homogeneously distributed cross-linking aids and/or antioxidants comprises heating polyethylene granulate to 85-95 degrees C in a fluid mixer at a high level of revs. per min., adding the additives in liquid form, then further heating up to 110 degrees C, and finally cooling immediately to 70 degrees C with further stirring. A suitable cross-linking aid is triallyl cyanurate (TAC) and pref. antioxidants are aromatic amines, phenols or organic phosphites. By using the mixer at about 3000 rpm the additives are worked into the granulated resin bodies without the surface becoming greasy or moist. Amts. up to 5% TAC can be added. Using liq. TAC mixed with highly dispersed silicic acid in ratio of 2:1, then 10% TAC can be worked in. If antioxidant is added simultaneously in ratio 1:1 then only a max. of 4% TAC can be added without effecting processing props. Cross-linked polyethylene is useful as insulation, for electric cables. The method gives homogeneous distribution of additives at low concn. as can be demonstrated by the even distribution of a slightly coloured additive.

Description

Dr. Fred Schimke Berlin, den 2O 7. 1975Dr. Fred Schimke Berlin, the 2 O 7. 1975

Frank HeilFrank Heil

Verfahren zur Herstellung von Zusatzstoffe enthaltendem PolyäthylenProcess for the production of polyethylene containing additives

Die Erfindung betrifft ein Verfahren zur Herstellung von Polyäthylen, welches Zusatzstoffe enthält, insbesondere Antioxidantien und/oder Vernetzerhilfen.The invention relates to a method of manufacture of polyethylene, which contains additives, in particular antioxidants and / or crosslinking aids.

Polyäthylen in vernetzter Form.findet als Isolierung elektrischer Leiter Verwehdung· Zur Erhöhung der Vernetzungsausbeute bei Einwirkung von energiereichen Strahlen oder organischen Peroxiden und Hitze werden ρolyfunktionelle Monomere in das Polyäthylen eingearbeitet. Zum Schutz des Polymeren gegen die abbauende Wirkung von Sauerstoff und Ozon bei hohen Temperaturen werden Antioxidantien zugesetzt.Polyethylene in cross-linked form is used as insulation electrical conductor twisting · To increase the crosslinking yield when exposed to high-energy rays or organic peroxides and heat Polyfunctional monomers incorporated into the polyethylene. To protect the polymer against degradation Effect of oxygen and ozone at high temperatures, antioxidants are added.

Als Vernetzerhilfe wird vorwiegend Tsiallyloyanurat (TAG), als Antioxidantien werden vorwiegend aromatische Amine, Phenole oder organische Phosphite verwendet« Ts iallyloyanurate (TAG) is predominantly used as a crosslinking aid, while aromatic amines, phenols or organic phosphites are predominantly used as antioxidants «

Beide Arten Zusatzstoffe müssen wegen ihres niedrigen Gehaltes im Polymeren sehr gleichmäßig verteilt werden. Dies wird üblicherweise erreicht, indem das in Granulatform vorliegende PE im Kneter und/oder auf der Walze aufgeschmolzen wird und die Zusätze in kleinen Dosen dem Polymeren zugemischt werden. Anschließend muß wieder granuliert werden.Both types of additives are required because of their low level Content can be distributed very evenly in the polymer. This is usually achieved by using the in Granulate form present PE in the kneader and / or on the The roller is melted and the additives are mixed into the polymer in small doses. Afterward must be granulated again.

Diese Verfahrensweise hat drei Nachteile. Für das Aufschmelzen des PE sind große Energien und lange Zeiten aufzuwenden. Weiterhin ist es schwierig, zu erreichen, die geringen Mengen Zusatz gleichmäßig einzuarbeiten, da einmal entstandene Konzentrationsanhäufungen kaum zu beseitigen sind. Zum dritten ist es wegen der schlechten Löslichkeit der Zusätze im PE sehr schwierig, die Zusätze überhaupt einzubringen. Uur bei entsprechend "This approach has three disadvantages. There are great energies and long times for melting the PE to spend. Furthermore, it is difficult to achieve evenly incorporating the small amounts of additive, there hardly any accumulations of concentration that have once arisen are to be eliminated. Thirdly, because of the poor solubility of the additives in PE, it is very difficult to obtain the To bring in additives at all. Uur with corresponding "

409S8 4/083 2409S8 4/083 2

kleiner Dosierung über lange Zeiten sind Konzentrationen bis ca. 1 % zu erreichen. Die Herstellung von masterbatches ist dadurch ganz ausgeschlossen.small doses over long periods of time, concentrations of up to approx. 1% can be achieved. The manufacture of masterbatches is completely excluded.

Außerdem hat dieses Verfahren den Nachteil, daß die so hergestellten Produkte gefürchtete Ausschwitzerscheinungen aufweisen und ein schmieriges Granulat darstellen, welches sich auf Extrudern nur unter starker Reduzierung der Ausstoßleistung verarbeiten läßt.In addition, this process has the disadvantage that the products produced in this way cause dreaded exudation phenomena have and represent a greasy granulate, which on extruders only under strong reduction the output can be processed.

Zweck der Erfindung ist es, ein Verfahren zu finden, nach welchem ohne besonderen Aufwand die Einarbeitung von Zusätzen in Polyäthylen vorgenommen werden kann·The purpose of the invention is to find a method according to which the incorporation of additives without any special effort can be made in polyethylene

Der Erfindung liegt die Aufgabe zugrunde, von der aufwendigen Kneter- und/oder tfalzentechnologie wegzukommen und durch ein einfacheres Verfahren , ohne besonderen technischen Aufwand, eine gute Einarbeitung sowie eine gute gleichmäßige Verteilung von Zusätzen in möglichst hoher Konzentration im Polyäthylen zu gewährleisten·The invention is based on the object of getting away from the complex kneading and / or folding technology and through a simpler process, without any special technical effort, good training and a good one to ensure uniform distribution of additives in the highest possible concentration in the polyethylene

Erfindungsgemäß wird handelsübliches PE-Granulat in einem Fluidmischer bei hoher Brehzahl des Rührers auf ^ 9O°C erwärmt, dann die Zusatzsubstanz in flüssiger Form zugesetzt und weiter gerührt bis zum Erreichen einer Temperatur von~110°0. Anschlit
abgekühlt und abgefüllt,
According to the invention, commercially available PE granulate is heated to ^ 90 ° C in a fluid mixer at high speed of the stirrer, then the additional substance is added in liquid form and the mixture is stirred further until a temperature of ~ 110 ° 0 is reached. Connection
cooled and bottled,

tür von~110°0. Anschließend wird unter Rühren auf 700Odoor from ~ 110 ° 0. Then, while stirring, to 70 0 O

Das Überraschende bei dieser Verfahrensweise ist, daß die Zusatzsubstanzen bei den relativ hohen Umdrehungszahlen des Mischwerkzeuges von 3·000 U/min in die Oberfläche der elastisch gewordenen Granulatkörner so eingearbeitet werden, daß die Oberfläche weder schmierig noch feucht wirkt;· Zusatz bis zu 5 % TAC ist nach diesem Verfahren möglich. Wird das verflüssigte TAG mit hochdisperser Kieselsäure im Verhältnis 2:1 gemischt, so können 10 % TAG noch in PE eingearbeitet werden, ohne daß infolge schmieriger Oberfläche der Granulatkörner ein Leistungsabfall beim Extrudieren eintritt·The surprising thing about this procedure is that the additional substances are worked into the surface of the granules that have become elastic at the relatively high speeds of rotation of the mixing tool of 3,000 rpm in such a way that the surface is neither greasy nor damp; Addition of up to 5 % TAC is possible according to this procedure. If the liquefied TAG is mixed with highly dispersed silica in a ratio of 2: 1, 10 % TAG can still be incorporated into PE without a drop in performance during extrusion due to the greasy surface of the granules.

9884/08 3 29884/08 3 2

Werden gleichzeitig mit TAC Antioxidantien zugesetzt,^ so kann bei einem Verhältnis lsi im allgemeinen nur eine Menge von maximal 4 % ohne Beeinträchtigung der ■Verarbeitungseigenschaften des PE-Granulats eingebracht werden.Antioxidants are added at the same time as TAC, ^ so with a ratio lsi can in general only an amount of max. 4% without impairing the ■ processing properties of the PE granulate will.

Durch die aufgezeigte Verfahrensweise ist es möglich, ohne großen technologischen Aufwand große Mengen üblicher Vernetzerhilfen und/oder Antioxidantien einzubringen. Besonders vorteilhaft wirkt sich die völlig gleichmäßige Verteilung der Zusätze selbst bei sehr kleinen Konzentrationen aus, wie an der gleichmäßigen Färbung der Granulatkörner bei Benutzung von schwach angefärbten Zusätzen leicht nachweisbar ist·The procedure shown makes it possible to use large quantities without great technological effort Bringing crosslinking aids and / or antioxidants. Which is particularly beneficial uniform distribution of the additives even with very low concentrations, as in the uniform color the granules are easily detectable when using slightly colored additives

Die Erfindung soll an einem Ausführungsbeispiel näher erläutert werden.The invention is intended to be based on an exemplary embodiment explained.

In einen 150 1 - Fluidmischer werden 40 kg PE vom Schmelzindex MFi; 0,5 in Granulatform eingebracht· Bei Rührgeschwindigkeiten von 3·000 U/min, werden nach Irreichen von~90°0 2 kg geschmolzenes TAG zugegeben. Es wird weiter gerührt, bis eine Temperatur von HO0C erreicht ist. Danach wird unter Rühren auf 700C abgekühlt und abgefüllt. Die gesamte Zyklusdauer beträgt a< 20 min. Es wird ein trockenes Granulat erhalten, welches den zugesetzten Vernetzer in gleichmäßiger Verteilung enthält·40 kg PE with a melt index MFi; 0.5 introduced in granulate form · At stirring speeds of 3,000 rpm, after reaching ~ 90 ° 0 2 kg of melted TAG are added. Stirring is continued until a temperature of HO 0 C is reached. It is then cooled to 70 ° C. while stirring and the mixture is filled. The total cycle time is a <20 min. A dry granulate is obtained which contains the added crosslinker in an even distribution.

409884/0832409884/0832

Claims (1)

Patentanspruch:Claim: Verfahren zur Herstellung von Polyäthylen, welches Yernetzerhilfen und/oder Antioxidantien in gleichmäßig verteilter Form enthält, dadurch gekennzeichnet, daß Polyäthylen-Granulat in einem Fluidmischer bei hoher Umdrehungszahl des Mischwerkzeuges auf 850O - 950O erhitzt wird, die Zusatzstoffe in flüssiger Form zugegeben werden und dann weiter bis auf rwii0°0 erhitzt und anschließend, unter weiterem Eühren sofort auf <700O abgekühlt wird.Process for the production of polyethylene which contains crosslinking aids and / or antioxidants in uniformly distributed form, characterized in that polyethylene granules are heated in a fluid mixer at high speed of the mixing tool to 85 0 - 95 0 O, the additives are added in liquid form and then further heated to rwii0 ° 0 and then immediately cooled to <70 0 O with further stirring. 40 9 8 8 4/083240 9 8 8 4/0832
DE19732354529 1973-07-06 1973-10-31 Polyethylene contg. homogeneously distributed additives - by high speed mixing of liquid additives with heated resin Withdrawn DE2354529A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DD17212873A DD115064A1 (en) 1973-07-06 1973-07-06

Publications (1)

Publication Number Publication Date
DE2354529A1 true DE2354529A1 (en) 1975-01-23

Family

ID=5491989

Family Applications (1)

Application Number Title Priority Date Filing Date
DE19732354529 Withdrawn DE2354529A1 (en) 1973-07-06 1973-10-31 Polyethylene contg. homogeneously distributed additives - by high speed mixing of liquid additives with heated resin

Country Status (2)

Country Link
DD (1) DD115064A1 (en)
DE (1) DE2354529A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0013752A1 (en) * 1979-01-18 1980-08-06 BASF Aktiengesellschaft Process for preparing finely divided polyolefine compositions with enhanced properties and their use in producing formed articles
EP0473922A1 (en) * 1990-09-05 1992-03-11 WERNER &amp; PFLEIDERER GUMMITECHNIK GMBH Method and device for mixing material with thermoplastic material

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0013752A1 (en) * 1979-01-18 1980-08-06 BASF Aktiengesellschaft Process for preparing finely divided polyolefine compositions with enhanced properties and their use in producing formed articles
EP0473922A1 (en) * 1990-09-05 1992-03-11 WERNER &amp; PFLEIDERER GUMMITECHNIK GMBH Method and device for mixing material with thermoplastic material

Also Published As

Publication number Publication date
DD115064A1 (en) 1975-09-12

Similar Documents

Publication Publication Date Title
DE2063395C3 (en) Thermosetting polyethylene mixture with an organic silicone additive
DE3038930C2 (en)
DE2430949A1 (en) PROCESS FOR MIXING POLYOLEFINS AND POLYDIORGANOSILOXAN GUM AND MIXTURES PREPARED HERE
DE1109366B (en) Process to improve the dimensional stability and solvent resistance of polyethylene
DE2631956B2 (en) Manufacture of arc-proof elastomers
IE43308B1 (en) Method and apparatus for forming chewing gum base and product
DE2424617B2 (en) Process for the controlled degradation of propylene polymers
DE2553094B2 (en) The use of certain per compounds to increase the resistance of ethylene polymers to charring and to increase the rate of hardening
DE1134198B (en) Process for the production of vulcanized elastomers
DE4443316A1 (en) Colorant preparation for the production of masterbatches
DE2737729C2 (en) Process for producing a crosslinkable polymer mixture in pellet form
DE2342486C2 (en) Process for the production of graft polymers
DE2354529A1 (en) Polyethylene contg. homogeneously distributed additives - by high speed mixing of liquid additives with heated resin
DE1116395B (en) Thermoplastic molding compound made of polyethylene and flame retardant compounds
AT240042B (en) Process for the production of new vulcanized products with high quality electrical and mechanical properties from mixtures of olefin copolymers
EP0494138B1 (en) Process for manufacturing plastic parts, in particular pipes, and diluted mixture for implementing the process
CN103435851B (en) Scented cellulosics and injection molding forming method thereof
DE2213202B2 (en) Process for the peroxidic crosslinking of polyethylene and / or ethylene copolymers
DE1569101B1 (en) Process for the production of blends from rubber and polyvinyl chloride
DE2554944A1 (en) Modified moisture-crosslinked thermoplastic rubbers - contain graftable cpds. e.g. silanes and/or are adducts formed with cpds. contg. e.g. silicon hydride gps.
DE602005002338T2 (en) Production process of lubricating oil additives with improved dimensional stability and increased low temperature performance
DE2949000A1 (en) METHOD FOR MIXING A HIGH VISCOSITY POLYDIORGANOSILOXANE AND AN ETHYLENE VINYL ACETATE COPOLYMER
DE1157390B (en) Process for the production of air-resistant, self-amalgamating organopolysiloxane compositions
DE1154620B (en) Process for crosslinking polyethylene compositions
DE2815817C2 (en) Process for conditioning powdery stabilizers for synthetic resins

Legal Events

Date Code Title Description
8141 Disposal/no request for examination