DE1226782B - Process for the production of molding compounds from polyethylene and carbon black - Google Patents
Process for the production of molding compounds from polyethylene and carbon blackInfo
- Publication number
- DE1226782B DE1226782B DEB80094A DEB0080094A DE1226782B DE 1226782 B DE1226782 B DE 1226782B DE B80094 A DEB80094 A DE B80094A DE B0080094 A DEB0080094 A DE B0080094A DE 1226782 B DE1226782 B DE 1226782B
- Authority
- DE
- Germany
- Prior art keywords
- carbon black
- polyethylene
- weight
- percent
- production
- 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
Links
- 229920000573 polyethylene Polymers 0.000 title claims description 27
- 239000006229 carbon black Substances 0.000 title claims description 26
- -1 polyethylene Polymers 0.000 title claims description 25
- 239000004698 Polyethylene Substances 0.000 title claims description 23
- 238000000465 moulding Methods 0.000 title claims description 15
- 238000000034 method Methods 0.000 title claims description 7
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 150000001875 compounds Chemical class 0.000 title description 11
- 239000012141 concentrate Substances 0.000 claims description 19
- 229920001577 copolymer Polymers 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 7
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 2
- 239000005977 Ethylene Substances 0.000 claims description 2
- 125000003262 carboxylic acid ester group Chemical class [H]C([H])([*:2])OC(=O)C([H])([H])[*:1] 0.000 claims 1
- 239000004071 soot Substances 0.000 description 6
- 239000000155 melt Substances 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical compound CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 description 3
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 229920001038 ethylene copolymer Polymers 0.000 description 3
- 239000003381 stabilizer Substances 0.000 description 3
- 239000001993 wax Substances 0.000 description 3
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- 125000005397 methacrylic acid ester group Chemical group 0.000 description 2
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pent‐4‐en‐2‐one Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 229920001567 vinyl ester resin Polymers 0.000 description 2
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 1
- 229920002367 Polyisobutene Polymers 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 125000005396 acrylic acid ester group Chemical group 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- DQXBYHZEEUGOBF-UHFFFAOYSA-N but-3-enoic acid;ethene Chemical compound C=C.OC(=O)CC=C DQXBYHZEEUGOBF-UHFFFAOYSA-N 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 150000001733 carboxylic acid esters Chemical class 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- AFSIMBWBBOJPJG-UHFFFAOYSA-N ethenyl octadecanoate Chemical compound CCCCCCCCCCCCCCCCCC(=O)OC=C AFSIMBWBBOJPJG-UHFFFAOYSA-N 0.000 description 1
- UIWXSTHGICQLQT-UHFFFAOYSA-N ethenyl propanoate Chemical compound CCC(=O)OC=C UIWXSTHGICQLQT-UHFFFAOYSA-N 0.000 description 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 1
- 229920006226 ethylene-acrylic acid Polymers 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 150000002688 maleic acid derivatives Chemical class 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/20—Compounding polymers with additives, e.g. colouring
- C08J3/22—Compounding polymers with additives, e.g. colouring using masterbatch techniques
- C08J3/226—Compounding polymers with additives, e.g. colouring using masterbatch techniques using a polymer as a carrier
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/02—Elements
- C08K3/04—Carbon
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions 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
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/06—Polyethene
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/28—Dissolving minerals other than hydrocarbons, e.g. by an alkaline or acid leaching agent
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised 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
- C08J2323/04—Homopolymers or copolymers of ethene
- C08J2323/06—Polyethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2423/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions 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
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/08—Copolymers of ethene
- C08L23/0846—Copolymers of ethene with unsaturated hydrocarbons containing atoms other than carbon or hydrogen
- C08L23/0853—Ethene vinyl acetate copolymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions 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
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/08—Copolymers of ethene
- C08L23/0846—Copolymers of ethene with unsaturated hydrocarbons containing atoms other than carbon or hydrogen
- C08L23/0869—Copolymers of ethene with unsaturated hydrocarbons containing atoms other than carbon or hydrogen with unsaturated acids, e.g. [meth]acrylic acid; with unsaturated esters, e.g. [meth]acrylic acid esters
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Physics & Mathematics (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Description
DEUTSCHESGERMAN
PATENTAMTPATENT OFFICE
AUSLEGESCHRIFTEDITORIAL
Int. CL:Int. CL:
Nummer: Aktenzeichen: Anmeldetag: Auslegetag:Number: File number: Registration date: Display day:
C08fC08f
Deutsche Kl.: 39 b-22/06 German class: 39 b -22/06
1226782
B80094IVc/39b
13. Januar 1965
13. Oktober 19661226782
B80094IVc / 39b
January 13, 1965
October 13, 1966
Es ist bekannt, daß sich in Polyäthylen erhebliche Mengen Ruß einarbeiten lassen. Dabei wird zunächst ein Konzentrat aus Polyäthylen und Ruß, beispielsweise mit HiKe eines Kneters oder Walzwerks, hergestellt und das Konzentrat dann homogen in Polyäthylen eingearbeitet.It is known that substantial amounts of carbon black can be incorporated into polyethylene. First of all a concentrate of polyethylene and carbon black, for example with the HiKe of a kneader or rolling mill and the concentrate is then incorporated homogeneously into polyethylene.
Der Umweg über ein Konzentrat ist für die gleichmäßige Verteilung des Rußes im Endprodukt erforderlich. Für die Herstellung des Konzentrates kann auch nach einem bekannten Verfahren eine Mischung verschiedener Polyolefine mit unterschiedlichem Kristallisationsgrad, z. B. Polyäthylen und Polyisobutylen, verwendet werden.The detour via a concentrate is necessary for the even distribution of the soot in the end product. For the production of the concentrate, a mixture of different can also be used according to a known method Polyolefins with different degrees of crystallization, e.g. B. polyethylene and polyisobutylene are used will.
Außerdem ist es bekannt (britische Patentschrift 890 426 und USA.-Patentschrift 2 512 459), Formmassen auf Basis von Polyäthylen, die feinteilige Feststoffe enthalten, herzustellen, indem man zunächst Konzentrate der Feststoffe in Wachsen, wie sie durch thermischen Abbau von Polyäthylen erhalten werden, gewinnt und die Konzentrate dann mit Polyäthylen ao vermischt. Diese bekannten Verfahren lassen jedoch vor allem im Hinblick auf die Gleichmäßigkeit der Verteilung des Rußes in den Formmassen zu wünschen übrig.It is also known (British Patent 890 426 and USA Patent 2 512 459), molding compounds on the basis of polyethylene, which contain finely divided solids, to be produced by first Concentrates of the solids in waxes, as they are obtained by the thermal degradation of polyethylene, wins and the concentrates then mixed with polyethylene ao. However, these known methods can be used especially with regard to the uniformity of the distribution of the carbon black in the molding compositions.
Es wurde nun gefunden, daß man Formmassen aus Polyäthylen und Ruß durch Einarbeiten eines Konzentrates des Rußes in einem Äthylenpolymerisat in das Polyäthylen vorteilhaft herstellen kann, wenn man als Äthylenpolymerisat ein Mischpolymerisat aus 50 bis 95 Gewichtsprozent Äthylen und 50 bis 5 Gewichtsprozent eines äthylenisch ungesättigten Carbonsäureesters verwendet.It has now been found that molding compositions made of polyethylene and carbon black can be produced by incorporating a concentrate of the carbon black in an ethylene polymer in the polyethylene can advantageously be produced if one as the ethylene polymer, a copolymer of 50 to 95 percent by weight of ethylene and 50 to 5 percent by weight an ethylenically unsaturated carboxylic acid ester is used.
Bei dem neuen Verfahren erhält man Formmassen, in denen der Ruß auch dann gleichmäßig im Polyäthylen verteilt ist, wenn man das Rußkonzentrat in das Polyäthylen unter Verwendung von Schnecken-Wellenmaschinen einarbeitet. Arbeitet man Rußkonzentrate beispielsweise auf Basis von Polyäthylen oder Wachsen unter Verwendung von Schneckenwellenmaschinen in bekannter Weise in Polyäthylen ein, so erhält man Formmassen, in denen der Ruß ungleichmäßig verteilt ist. Dünnschnitte, die aus solchen bekannten Formmassen hergestellt sind, weisen Schlieren auf, und es können darin mikroskopisch Rußagglomerate beobachtet werden.The new process gives molding compounds in which the carbon black is evenly distributed in the polyethylene is distributed when you add the carbon black concentrate to the polyethylene using screw and shaft machines incorporated. If you work, for example, based on polyethylene or carbon black concentrates Wax in polyethylene in a known manner using worm shaft machines, see above molding compounds are obtained in which the carbon black is unevenly distributed. Thin sections that are known from such Molding compositions are produced, have streaks, and there can be microscopic carbon black agglomerates therein to be observed.
Das Verfahren ist zur Herstellung von Ruß enthaltenden Formmassen aus den üblichen hochmolekularen Polyäthylenen geeignet, die nach Hoch- und Niederdruckpolymerisationsverfahren hergestellt sein können und die im allgemeinen Molekulargewichte (gemessen nach Überreiter, Macromolekulare Chemie, Bd. 8 [1952], S. 21 bis 28) über 10 000 aufweisen. The process is for the production of molding compounds containing carbon black from the usual high molecular weight Polyethylenes are suitable, which are produced by high and low pressure polymerization processes can and the general molecular weights (measured according to Überreiter, Macromolekulare Chemie, Vol. 8 [1952], pp. 21 to 28) over 10,000.
Verfahren zur Herstellung von Formmassen aus
Polyäthylen und RußProcess for the production of molding compounds
Polyethylene and carbon black
Anmelder:Applicant:
Badische Anilin- & Soda-FabrikAniline & Soda Factory in Baden
Aktiengesellschaft, Ludwigshafen/RheinAktiengesellschaft, Ludwigshafen / Rhein
Als Erfinder benannt:Named as inventor:
Dr. Klaus Böttcher, Wesseling;Dr. Klaus Böttcher, Wesseling;
Dr. Wolfgang Immel,Dr. Wolfgang Immel,
Dr. Klaus Kinkel, Ludwigshafen/Rhein;Dr. Klaus Kinkel, Ludwigshafen / Rhine;
Dr. Friedrich Urban, LimburgerhofDr. Friedrich Urban, Limburgerhof
Als Äthylenmischpolymerisate sind vor allem solche aus Vinylestern, Acrylsäureestern und/oder Methacrylsäureestern geeignet. Als Vinylester kommen z. B. Vinylacetat und Vinylpropionat sowie ferner Vinylstearat in Frage. Die geeigneten Acryl- und Methacrylsäureester leiten sich besonders von Alkanolen mit 1 bis 4 Kohlenstoffatomen, wie Methanol, Äthanol, Propanol, Isopropanol und tert.-Butylalkohol, ab. Ferner kommen für die Mischpolymerisate als Komponente Maleinsäureester, ζ. B. der Diäthylester, in Betracht. Vorgezogen werden Äthylenmischpolymerisate, die Vinylacetat und/oder Acrylsäureäthylester einpolymerisiert enthalten. Die Mischpolymerisate enthalten 5 bis 50 Gewichtsprozent äthylenisch ungesättigte Monocarbonsäureester einpolymerisiert und weisen meist bei 19O0C Schmelzindizes zwischen 0,1 und 100 auf. Besonders gute Ergebnisse werden mit Äthylenmischpolymerisaten erzielt, die 20 bis 25 Gewichtsprozent an äthylenisch ungesättigten Monocarbonsäureester einpolymerisiert enthalten. Für die Rußkonzentrate können auch mehrere Mischpolymerisate der genannten Art eingesetzt werden.Particularly suitable ethylene copolymers are those composed of vinyl esters, acrylic acid esters and / or methacrylic acid esters. As vinyl esters, for. B. vinyl acetate and vinyl propionate and also vinyl stearate in question. The suitable acrylic and methacrylic acid esters are derived in particular from alkanols having 1 to 4 carbon atoms, such as methanol, ethanol, propanol, isopropanol and tert-butyl alcohol. Maleic acid esters, ζ, are also used as components for the copolymers. B. the diethyl ester into consideration. Ethylene copolymers which contain vinyl acetate and / or ethyl acrylate in polymerized form are preferred. The copolymers contain from 5 to 50 weight percent ethylenically unsaturated Monocarbonsäureester copolymerized units and have usually at 19O 0 C melt indexes between 0.1 and 100 on. Particularly good results are achieved with ethylene copolymers which contain 20 to 25 percent by weight of ethylenically unsaturated monocarboxylic acid ester as polymerized units. Several copolymers of the type mentioned can also be used for the carbon black concentrates.
Der Rußgehalt des Konzentrates beträgt im allgemeinen 5 bis 50 Gewichtsprozent, vorzugsweise 30 bis 35 Gewichtsprozent. Es können die üblichen Rußsorten verwendet werden, die meist eine Teilchengröße um 25 ηιμ haben. Besonders bewährt haben sich Gasruß und Ofenruß.The carbon black content of the concentrate is generally 5 to 50 percent by weight, preferably 30 to 35 weight percent. The usual types of carbon black can be used, mostly one particle size to have 25 ηιμ. Gas black have proven particularly useful and furnace soot.
Die Rußkonzentrate können in üblicher Weise stabilisiert sein, wobei der Gehalt des Konzentrates an Stabilisator im allgemeinen zwischen 0,01 und 5 Gewichtsprozent, vorzugsweise zwischen 0,1 und 1 Gewichtsprozent, liegt.The carbon black concentrates can be stabilized in the usual way, the content of the concentrate being Stabilizer generally between 0.01 and 5 percent by weight, preferably between 0.1 and 1 percent by weight, lies.
609 670/447609 670/447
Die Rußkonzentrate können in das Polyäthylen in üblicher Weise unter Verwendung von Knetern; Walzwerken, Schneckenwellenextrudern oder Scheibenknetern eingearbeitet oder gegebenenfalls einem Strom von geschmolzenem Polyäthylen zugesetzt werden.The carbon black concentrates can be mixed into the polyethylene in the usual way using kneaders; Rolling mills, Incorporated screw-shaft extruders or disk kneaders or optionally a stream of molten polyethylene can be added.
Die in den folgenden Beispielen angegebenen Teile sind Gewichtsteile. ; . := . ■. ...The parts given in the following examples are parts by weight. ; . : = . ■. ...
In einem handelsüblichen Stempelkneter; "Werden 65,4 Teile eines Äthylen-Vinylacetat-Mischcopolymerisates des Schmelzindex 20, das 20 Gewichtsprozent Vinylacetat einpolymerisiert enthält, mit 13,5 Teilen Gasruß, 20,5 Teilen Ofenruß und 0,66 Teilen eines handelsüblichen Stabilisators 5 Minuten bei 15O0C ge- *5 knetet und die Mischung nach dem Erkalten granuliert. Das Granulat wird in einem Extruder mit geschmolzenem Polyäthylen der Dichte 0,918 und des Schmelzindex 0,5 in einer Menge gemischt, daß der Rußgehalt in der fertigen Formmasse 2 Gewichtsprozent beträgt:" Ein "Dünnschnitt" desr Produktes zeigt unter dem Mikroskop gleichmäßige Verteilung des Rußes. . ■In a standard stamp kneader ; "Will 65.4 parts of an ethylene-vinyl acetate Mischcopolymerisates copolymerized form in the melt index 20, 20 percent by weight vinyl acetate, 13.5 parts of carbon black, 20.5 parts of furnace carbon black and 0.66 parts of a commercial stabilizer ge 5 minutes at 15O 0 C - * 5 kneads and the mixture is granulated after cooling. The granulate is mixed in an extruder with melted polyethylene with a density of 0.918 and a melt index of 0.5 in an amount such that the carbon black content in the finished molding compound is 2 percent by weight: "A" thin section The product shows even distribution of the soot under the microscope. . ■
Verwendet man an Stelle des Mischpolymerisates für das Konzentrat die gleiche Menge Polyäthylen der Dichte 0,918 und des Schmelzindex 1,5, so erhält man · unter sonst gleichen Bedingungen eine Formmasse, in der der Ruß Schlieren und Agglomerate bildet.If the same amount of polyethylene is used instead of the copolymer for the concentrate Density 0.918 and the melt index 1.5, one obtains under otherwise identical conditions, a molding compound in which the soot forms streaks and agglomerates.
Verwendet man an Stelle des Mischpolymerisates für das Konzentrat die gleiche Menge eines Äthylen-Propylen-Mischpolymerisates gemäß der USA.-Patentschrift 3 137 672 (Beispiel 1, Zeilen 25 bis 28), so erhält man unter sonst gleichen Bedingungen ebenfalls eine Formmasse, in der der Ruß in ungleichmäßiger Verteilung vorliegt.If the same amount of an ethylene-propylene copolymer is used instead of the copolymer for the concentrate according to U.S. Patent 3,137,672 (Example 1, lines 25-28) so obtained under otherwise identical conditions, a molding compound is also used in which the carbon black is unevenly distributed is present.
Verwendet man an Stelle des Mischpolymerisates für das Konzentrat die gleiche Menge eines Gemisches aus 75 Teilen'eines Äthyleri-Pröpylen-Mischpolymerisates und 30 Teilen eines Polypropylenwachses gemäß den ausgelegten Unterlagen" des belgischen Patents 626 813 (Beispiel 1, erster Satz), so erhält man unter sonst gleichen Bedingungen eine Formmasse; in der der Ruß Agglomerate bildet.If the same amount of a mixture is used instead of the copolymer for the concentrate from 75 parts of a Ethyleri-Propylene copolymer and 30 parts of a polypropylene wax according to the laid-open documents "of the Belgian patent 626 813 (example 1, first sentence), a molding compound is obtained under otherwise identical conditions; in the the soot forms agglomerates.
65,4 Teile eines Äthylen-Acrylsäureäthylester-Mischpolymerisates des Schmelzindex 20, das 20 Gewichtsprozent Acrylsäureäthylester einpolymerisiert enthält, wird — wie im Beispiel 1 angegeben — mit Ruß und Stabilisator vermischt und das erhaltene Konzentrat in einer Schneckenwellenmaschme mit geschmolzenem Polyäthylen derart vermischt, daß der Rußgehalt in der fertigen Formmasse 2 Gewichtsprozent beträgt. Ein Dünnschnitt des Produktes zeigt unter dem Mikroskop gleichmäßig braune Farbe; Schlieren und Rußagglomerate können nicht beobachtet werden.65.4 parts of an ethylene-acrylic acid ethyl ester copolymer the melt index 20, which contains 20 percent by weight of ethyl acrylate polymerized, is - as indicated in Example 1 - mixed with carbon black and stabilizer and the concentrate obtained mixed in a worm shaft machine with molten polyethylene in such a way that the carbon black content in of the finished molding compound is 2 percent by weight. A thin section of the product shows under the microscope uniform brown color; Streaks and soot agglomerates cannot be observed.
Claims (1)
Ausgelegte Unterlagen des belgischen Patents Nr. 626 813;
USA.-Patentschrift Nr. 3 137 672.Considered publications:
Opened documents of Belgian patent No. 626 813;
U.S. Patent No. 3,137,672.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEB80094A DE1226782B (en) | 1965-01-13 | 1965-01-13 | Process for the production of molding compounds from polyethylene and carbon black |
| FR45663A FR1463502A (en) | 1965-01-13 | 1966-01-12 | Manufacturing process of polyethylene and carbon black molding materials |
| GB138766A GB1125571A (en) | 1965-01-13 | 1966-01-12 | Production of moulding materials from polyethylene and carbon black |
| BE675059D BE675059A (en) | 1965-01-13 | 1966-01-13 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEB80094A DE1226782B (en) | 1965-01-13 | 1965-01-13 | Process for the production of molding compounds from polyethylene and carbon black |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE1226782B true DE1226782B (en) | 1966-10-13 |
Family
ID=6980578
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DEB80094A Pending DE1226782B (en) | 1965-01-13 | 1965-01-13 | Process for the production of molding compounds from polyethylene and carbon black |
Country Status (4)
| Country | Link |
|---|---|
| BE (1) | BE675059A (en) |
| DE (1) | DE1226782B (en) |
| FR (1) | FR1463502A (en) |
| GB (1) | GB1125571A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4767804A (en) * | 1983-08-03 | 1988-08-30 | Rubber Bands And Plastic Research Association Of Great Britain | Control of transformations within polymers and products thereof |
| US5053444A (en) * | 1986-09-01 | 1991-10-01 | Imperial Chemical Industries Plc | Polymer additive concentrate |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2741005A1 (en) * | 1977-09-12 | 1979-03-15 | Basf Ag | USE OF A SOOT CONCENTRATE BASED ON AN ETHYLENE COPOLYMERISATE FOR THE PRODUCTION OF POLYAETHYLENE MOLDING COMPOUNDS FOR TUBES |
| SE8303538L (en) * | 1983-06-20 | 1984-12-21 | Unifos Kemi Ab | COMPOSITIONS CONTAINING LINES POLYETTE AND COPOLYMERS OF ONE AND ACRYLATE |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE626813A (en) * | 1958-01-30 | 1963-07-04 | ||
| US3137672A (en) * | 1962-02-01 | 1964-06-16 | Hercules Powder Co Ltd | Impact strength of blends of polyethylene and polypropylene |
-
1965
- 1965-01-13 DE DEB80094A patent/DE1226782B/en active Pending
-
1966
- 1966-01-12 FR FR45663A patent/FR1463502A/en not_active Expired
- 1966-01-12 GB GB138766A patent/GB1125571A/en not_active Expired
- 1966-01-13 BE BE675059D patent/BE675059A/xx not_active IP Right Cessation
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE626813A (en) * | 1958-01-30 | 1963-07-04 | ||
| US3137672A (en) * | 1962-02-01 | 1964-06-16 | Hercules Powder Co Ltd | Impact strength of blends of polyethylene and polypropylene |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4767804A (en) * | 1983-08-03 | 1988-08-30 | Rubber Bands And Plastic Research Association Of Great Britain | Control of transformations within polymers and products thereof |
| US5053444A (en) * | 1986-09-01 | 1991-10-01 | Imperial Chemical Industries Plc | Polymer additive concentrate |
| US5516814A (en) * | 1986-09-01 | 1996-05-14 | Imperial Chemical Industries Plc | Process for preparing a polymer concentrate |
Also Published As
| Publication number | Publication date |
|---|---|
| BE675059A (en) | 1966-07-13 |
| FR1463502A (en) | 1966-12-23 |
| GB1125571A (en) | 1968-08-28 |
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