DE1007999B - Process for the production of solid ethylene polymers - Google Patents

Process for the production of solid ethylene polymers

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Publication number
DE1007999B
DE1007999B DEB36947A DEB0036947A DE1007999B DE 1007999 B DE1007999 B DE 1007999B DE B36947 A DEB36947 A DE B36947A DE B0036947 A DEB0036947 A DE B0036947A DE 1007999 B DE1007999 B DE 1007999B
Authority
DE
Germany
Prior art keywords
production
ethylene polymers
ethylene
solid
solid ethylene
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
DEB36947A
Other languages
German (de)
Inventor
Renee Bodmer
Dr Heinrich Hopff
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.)
BASF SE
Original Assignee
BASF SE
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
Priority to IT558047D priority Critical patent/IT558047A/it
Application filed by BASF SE filed Critical BASF SE
Priority to DEB36947A priority patent/DE1007999B/en
Publication of DE1007999B publication Critical patent/DE1007999B/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
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond

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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)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

Verfahren zur Herstellung von festen Äthylenpolymerisaten Die Herstellung von öligen Polymerisaten des Äthylens durch Umsetzung von Äthylen mit wasserfreiem Aluminiumchlorid als Katalysator ist schon verschiedentlich in der Literatur beschrieben wanden. Auch die Bildung von Gemischen aus festen und öligen Äthyl.enpalymerisaten mit Hilfe von Aluminiumchlorid, das mit Titantetrachlorid aktiviert ist, ist bereits bekannt. Dabei wird Äthylen mit dem Katalysator unter Druck und bei erhöhter Temperatur, z. B. unter 58 atü und bei 135°, umgesetzt.Process for the production of solid ethylene polymers The production of oily polymers of ethylene by reacting ethylene with anhydrous Aluminum chloride as a catalyst has already been described variously in the literature wound. Also the formation of mixtures of solid and oily Ethyl.enpalymerisaten with the help of aluminum chloride activated with titanium tetrachloride is already known. Here, ethylene is combined with the catalyst under pressure and at elevated temperature, z. B. under 58 atmospheres and at 135 ° implemented.

Es wurde nun gefunden, daß sich Äthylen mit Aluminiumchlorid allein in Gegenwart von niedrigsiedenden organischen Lösungs- oder Verdünnungsmitteln drucklos oder unter mäßigen Drücken bei Temperaturen, die unterhalb des Siedepunktes des Lösungs- bzw. Verdünnungsmittels liegen, in feste Polymerisate überführen läßt, ohne daß sich ölige Nebenprodukte bilden.It has now been found that ethylene reacts with aluminum chloride alone pressureless in the presence of low-boiling organic solvents or diluents or under moderate pressures at temperatures below the boiling point of the Solvent or diluent can be converted into solid polymers, without the formation of oily by-products.

Die Reaktion wird in der Weise ausgeführt, daß man feingepulvertes wasserfreies Aluminiumchlorid in den ni.edrigsiedenden Lösungs- oder Verdünnungsmitteln, die gegebenenfalls unter mäßig erhöhtem Druck stehen, z. B. in Butan, Pentan, Hexen, Petroläther, Methy lenchlorid oder Tetrachlorkohlenstoff, suspendiert und durch diese Suspension einen feinverteilten Äthylenstram bei Temperaturen zwischen etwa -30 und + 30° hindurchleitet. Es entsteht dabei langsam eine zähe, braune Masse. Das in ihr enthaltene A1 Cl, wird mach dem Dekantieren, der flüssigen Phase mit Eis zersetzt. Durch Extraktion des Rückstandes mit Lösungsmitteln, wie Äther, und navhherigem Verdampfen des Lösungsmittels wird ein festes, schneenveißes Polyäthylen vom Erweichungspunkt 128 bis 130° erhalten.The reaction is carried out in such a way that one finely powdered anhydrous aluminum chloride in the low-boiling solvents or thinners, which are optionally under moderately increased pressure, z. B. in butane, pentane, hexene, Petroleum ether, methylene chloride or carbon tetrachloride, suspended and through this suspension a finely divided Äthylenstram at temperatures between about -30 and + 30 °. A tough, brown mass slowly develops. The A1 Cl contained in it becomes part of the decanting, the liquid phase Ice decomposes. By extracting the residue with solvents such as ether, and Upon evaporation of the solvent, a solid, snow-white polyethylene becomes obtained from the softening point 128 to 130 °.

Sein Malekulargew icht hängt von der angewandten Temperatur ab. Bei tiefen Temperaturen erhält man höhere Malekulargewichte, bei höheren Temperaturen dagegen niedrigere Malekulargewichte. Das Molekulargewicht kann in weiten Grenzen verändert werden.His molecular weight depends on the temperature used. at At low temperatures you get higher molecular weights, at higher temperatures on the other hand, lower molecular weights. The molecular weight can be within wide limits to be changed.

Die weniger hocbmodekula,ren Palyäthylene sind als Austauschp,rod.ukte für Wachse und die Produkte mit höheren Malekulargewichten a:ls Kunststoffe verwendbar.The less hocbmodekula, ren paläthylenes are as exchange products Can be used for waxes and products with higher molecular weights a: ls plastics.

Die in den Beispielen genannten Teile sind Gewichtsteile.The parts mentioned in the examples are parts by weight.

Beispiel 1 10 Teile feingepulvertes, handelsübliches Aluminiumchlarid werden mit 200 Teilen Petroläther in einem 2 m hohen Rohr suspendiert. Man leitet nun mehrere Stunden durch eine am Boden des Rohres angebrachte Glasfritte einen feinverteilten Äthylelstrom ein. Das Äthylen wird zu ungefähr 28 % umgesetzt. Nach, dem Absetzen der festen Bestandteile wird die flüssige Phase dekantiert; der halbfeste Rückstand mit Eis zersetzt und mit Äther erschöpfend extrahiert. Nach dem Verdampfen des Äthers erhält man das gebildete Polyäthylen als schneeweißen Rückstand vom Erweichungspunkt 128°.Example 1 10 parts of finely powdered, commercially available aluminum chloride are suspended with 200 parts of petroleum ether in a 2 m high tube. Man directs now for several hours through a glass frit attached to the bottom of the tube a finely divided ethyl stream. About 28% of the ethylene is converted. To, The liquid phase is decanted after the solid constituents have settled; the semi-solid The residue is decomposed with ice and exhaustively extracted with ether. After evaporation of the ether, the polyethylene formed is obtained as a snow-white residue from the softening point 128 °.

Das dekantierte Lösungsmittel kann für einen neuen Ansatz verwendet werden.The decanted solvent can be used for a new batch will.

Zum Vergleich werden 10 Teile feingepulvertes, handelsübliches Aluminiumchlo@ri@d in 200 Teilen Äthylenchlorid in einem 2 m hohen Rohr suspendiert. Hierauf leitet man 3 Stunden Äthylen bei Raumtemperatur ein. Das Aluminiumchlorid geht hierbei vollständig in Lösung. Das Reaktionsprodukt wird anschließend mit Eis behandelt. Nach Abd estillieren des Äthylenchlarids erhält man ausschließlich ein dünnflüssiges, braungefärbtes C51 als Rückstand.For comparison, 10 parts of finely powdered, commercially available aluminum chloride are used suspended in 200 parts of ethylene chloride in a 2 m high tube. On this leads one 3 hours of ethylene at room temperature. The aluminum chloride goes here completely in solution. The reaction product is then treated with ice. After distilling off the ethylene chloride, only a thin liquid, brown colored C51 as residue.

Beispiel 2 10 Teile feingepulvertes, handelsübliches Aluminiumchlorid werden in 150 Teilen Methylenchlarid suspendiert. In dieser Suspension setzt man bei 20° Äthylen gemäß Beispiel 1 um. Man erhält festes Polyäthylen vom Erweiohungspunkt 125' in einer Ausbeute von 40 0/0.Example 2 10 parts of finely powdered, commercially available aluminum chloride are suspended in 150 parts of methylene chloride. Ethylene according to Example 1 is reacted in this suspension at 20.degree. Solid polyethylene with an expansion point of 125 'is obtained in a yield of 40%.

Claims (1)

PATENTANSPRUCH: Verfahren zur Herstellung von festen Äthylenpolymerisaten in organischen Lösungsmitteln mit Hilfe von Alurniniumehlozid als Katalysator, dadurch gekennzeichnet, daß in Gegenwart von organischen Lösungs- oder Verdünnungsmitteln mit Siedepunkten bis zu 77° bei Temperaturen unterhalb des Siedepunktes des Lösungs- oder Verdünnungsmittels, gegebenenfalls unter mäßigem Druck, polymerisiert wird. In Betracht gezogene Druckschriften: USA.-Patentschrift Nr. 2183154. PATENT CLAIM: A process for the preparation of solid ethylene polymers in organic solvents with the aid of Alurniniumehlozid as a catalyst, characterized in that in the presence of organic solvents or diluents with boiling points up to 77 ° at temperatures below the boiling point of the solvent or diluent, optionally under moderate Pressure being polymerized. References considered: U.S. Patent No. 2183154.
DEB36947A 1955-08-23 1955-08-23 Process for the production of solid ethylene polymers Pending DE1007999B (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
IT558047D IT558047A (en) 1955-08-23
DEB36947A DE1007999B (en) 1955-08-23 1955-08-23 Process for the production of solid ethylene polymers

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEB36947A DE1007999B (en) 1955-08-23 1955-08-23 Process for the production of solid ethylene polymers

Publications (1)

Publication Number Publication Date
DE1007999B true DE1007999B (en) 1957-05-09

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DEB36947A Pending DE1007999B (en) 1955-08-23 1955-08-23 Process for the production of solid ethylene polymers

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DE (1) DE1007999B (en)
IT (1) IT558047A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3049526A (en) * 1958-03-04 1962-08-14 Dal Mon Research Co Polymerization process
US3054788A (en) * 1958-03-04 1962-09-18 Dal Mon Research Co Polymerization process
US3054784A (en) * 1958-08-07 1962-09-18 Monsanto Chemicals Polymerisation processes
US3056770A (en) * 1958-03-04 1962-10-02 Dal Mon Research Co Polymerization process
US3057842A (en) * 1958-03-17 1962-10-09 Monsanto Chemicals Alcl3-catalyzed polymerization of ethylene
US3065217A (en) * 1958-03-04 1962-11-20 Dal Mon Research Co Polymerization process
US3098828A (en) * 1957-11-04 1963-07-23 Dal Mon Research Co Catalyst prepared by grinding zirconium and aluminum chloride
US3158593A (en) * 1958-04-24 1964-11-24 Monsanto Co Aluminum chlorofluoride polymerization catalysts
US3159607A (en) * 1958-05-20 1964-12-01 Dal Mon Research Co Polymerization process

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2183154A (en) * 1935-09-19 1939-12-12 Consortium Elektrochem Ind Process for producing polymerization products of ethylene

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2183154A (en) * 1935-09-19 1939-12-12 Consortium Elektrochem Ind Process for producing polymerization products of ethylene

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3098828A (en) * 1957-11-04 1963-07-23 Dal Mon Research Co Catalyst prepared by grinding zirconium and aluminum chloride
US3049526A (en) * 1958-03-04 1962-08-14 Dal Mon Research Co Polymerization process
US3054788A (en) * 1958-03-04 1962-09-18 Dal Mon Research Co Polymerization process
US3056770A (en) * 1958-03-04 1962-10-02 Dal Mon Research Co Polymerization process
US3065217A (en) * 1958-03-04 1962-11-20 Dal Mon Research Co Polymerization process
US3057842A (en) * 1958-03-17 1962-10-09 Monsanto Chemicals Alcl3-catalyzed polymerization of ethylene
US3158593A (en) * 1958-04-24 1964-11-24 Monsanto Co Aluminum chlorofluoride polymerization catalysts
US3159607A (en) * 1958-05-20 1964-12-01 Dal Mon Research Co Polymerization process
US3054784A (en) * 1958-08-07 1962-09-18 Monsanto Chemicals Polymerisation processes
US3080349A (en) * 1958-08-07 1963-03-05 Monsanto Chemicals Polymerization with the aid of a catalyst containing aluminum halide and an organo-mercury compound in a halogenated liquid medium

Also Published As

Publication number Publication date
IT558047A (en)

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