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DE1058257B - Process for the preparation of polymerization products - Google Patents

Process for the preparation of polymerization products

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Publication number
DE1058257B
DE1058257B DEB35887A DEB0035887A DE1058257B DE 1058257 B DE1058257 B DE 1058257B DE B35887 A DEB35887 A DE B35887A DE B0035887 A DEB0035887 A DE B0035887A DE 1058257 B DE1058257 B DE 1058257B
Authority
DE
Germany
Prior art keywords
parts
preparation
mixtures
metals
polymerization products
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
DEB35887A
Other languages
German (de)
Inventor
Dr Hans-Martin Weitz
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
Application filed by BASF SE filed Critical BASF SE
Priority to DEB35887A priority Critical patent/DE1058257B/en
Publication of DE1058257B publication Critical patent/DE1058257B/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
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/46Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides selected from alkali metals
    • 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
    • C08F4/00Polymerisation catalysts
    • C08F4/06Metallic compounds other than hydrides and other than metallo-organic compounds; Boron halide or aluminium halide complexes with organic compounds containing oxygen
    • 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
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (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

Zierfahren zur Herstellung von Polymerisationsprodukten Es wurde gefunden, daß man olefinisch ungesättigte Verbindungen mit Hilfe von Anlagerungsverbindungen von Metallen oder Gemischen aus Metallen und Metallhalogeniden an I-#,etone zu hochmolekularen Verbindungen umsetzen kann. Hierbei können gegebenenfalls zusätzlich Zn C12, A1 C13, Fe C13, Si C14, Ti Cl 4 oder Äthylchlorid, Chloroform, Tetrachlorkohlenstoff, Dichloräthan, Hexachloräthan, Trichlorbrommethan, Trifluorjodmethan, tert.-Butylchlorid, Triphenylehlormethan, Trichloracetonitril oder Benzotrichlorid oder deren Gemische verwendet werden.Decorative processes for the production of polymerization products It was found that you can olefinically unsaturated compounds with the help of addition compounds from metals or mixtures of metals and metal halides to I - #, etones to high molecular weight Can implement connections. Here, if necessary, Zn C12, A1 C13, Fe C13, Si C14, Ti Cl 4 or ethyl chloride, chloroform, carbon tetrachloride, Dichloroethane, hexachloroethane, trichlorobromomethane, trifluoroiodomethane, tert-butyl chloride, Triphenyl chloromethane, trichloroacetonitrile or benzotrichloride or mixtures thereof be used.

Geeignete olefinisch ungesättigte Verbindungen sind z. B. Monoolefine, wie Äthylen, Propylen, Isobutylen, sowie Diolefine, z. B. Butadien und Isopren; ferner Styrol und seine Alkyl- und Halogenderivate, Vinylverbindungen, wie Vinylchlorid, Vinylidenchlorid, Allylalkohol, Vinyläther, Vinylester, Acrylester, Acrylnitril, Tetrafluoräthylen, Trifluorchloräthylen oder Gemische dieser Monomeren.Suitable olefinically unsaturated compounds are, for. B. monoolefins, such as ethylene, propylene, isobutylene, and diolefins, e.g. B. butadiene and isoprene; also styrene and its alkyl and halogen derivatives, vinyl compounds such as vinyl chloride, Vinylidene chloride, allyl alcohol, vinyl ether, vinyl ester, acrylic ester, acrylonitrile, Tetrafluoroethylene, trifluorochloroethylene or mixtures of these monomers.

Als Katalysatoren eignen sich z. B. die Anlagerungsv erbindungen der Alkalimetalle an Ketone, also die sogenannten Metallketyle der Formel Me-(Keton)n, in der Me@Metall und n z. B. 1, 1,5, 2 oder 3 ist. Geeignete Ketone sind z. B. Benzophenon, Phenylbiphenylketon, Hexamethylaceton, Michlers Keton, y-Pyron, Fluorenon, Xanthon oder Phenanthrenchinon. Ferner sind geeignet die Alkalisubstitutionsprodukte der Pinakone der Formel in der R=-C (Alkyl)3 oder Aryl ist, die sich bei der Einwirkung beispielsweise von Natriumalkoholat oder Natriumamid auf Pinakone bilden und mit den Ketylen im Gleichgewicht stehen. Auch die Verbindungen, die bei der Reaktion von Gemischen aus Metallen und Metallhalogeniden mit Ketonen entstehen, können verwendet werden, z. B. Gemische aus Magnesium und Magnesiumjodid, Beryllium und Bervlliumjodid oder Zink und Zinkhalogenid.Suitable catalysts are, for. B. the Anlagungsv connections of the alkali metals to ketones, so the so-called metal ketyls of the formula Me- (ketone) n, in the Me @ metal and n z. B. 1, 1.5, 2 or 3 is. Suitable ketones are e.g. B. benzophenone, phenylbiphenyl ketone, hexamethylacetone, Michler's ketone, γ-pyrone, fluorenone, xanthone or phenanthrenequinone. The alkali substitution products of the pinacones of the formula are also suitable in which R = -C (alkyl) 3 or aryl, which are formed on the action of, for example, sodium alcoholate or sodium amide on pinacones and are in equilibrium with the ketylenes. The compounds formed in the reaction of mixtures of metals and metal halides with ketones can also be used, e.g. B. Mixtures of magnesium and magnesium iodide, beryllium and beryllium iodide or zinc and zinc halide.

Die Reaktionstemperatur liegt zwischen 20 und 200° C und höher, die Drücke je nach Art des Olefins und der Reaktionstemperatur beim Dampfdruck oder höher.The reaction temperature is between 20 and 200 ° C and higher, the Pressures depending on the type of olefin and the reaction temperature at vapor pressure or higher.

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

Beispiel 1 In einem Schüttelautoklav werden 5 Teile Phenylbiphenylketon und 10 Teile einer Kalium-Natrium-Legierung (7,7:2,3) in 240 Teilen Cyclohexan auf 100°C erwärmt. Nach Erreichen dieser Temperatur wird Äthylen, das 1 Volumprozent Äthylenchlorid enthält, unter einem Druck von 100 atü eingepreßt. Die Äthylenaufnahme ist nach 2 Stunden beendet. Nach Abkühlen, Entspannen und Zersetzen des überschüssigen Alkalimetalls durch :Methanol wird das entstandene Polyäthylen abfiltriert, gewaschen und getrocknet. Man erhält 16 Teile eines bei 135° C schmelzenden Produktes. Das Filtrat enthält etwa die doppelte Menge flüssiger Hochpolymerer, deren untere Siedegrenze bei Normaldruck oberhalb 250° C liegt. Beispiel 2 100 Teile frisch destilliertes Styrol, 200 Teile Cyclohexan, 5 Teile Phenylbiphenylketon und 2 Teile Kalium werden @lz Stunde bei 65° C unter Stickstoff gerührt. Anschließend leitet man 0,5 Teile Tetrachlorkohlenstoff ein. Nach einer Stunde wird die Reaktionsmischung abgekühlt und langsam mit 1000 Teilen Methanol versetzt. Das abgeschiedene Polystyrol wird abfiltriert, mit methanolischer Salzsäure und mit Methanol gewaschen und getrocknet. ;Man erhält 70 Teile schwach gelbliches Polystyrol.Example 1 5 parts of phenylbiphenyl ketone are used in a shaking autoclave and 10 parts of a potassium-sodium alloy (7.7: 2.3) in 240 parts of cyclohexane 100 ° C heated. When this temperature is reached, ethylene becomes 1 percent by volume Contains ethylene chloride, injected under a pressure of 100 atü. The ethylene intake ends after 2 hours. After cooling down, relaxing and decomposing the excess Alkali metal by: methanol, the resulting polyethylene is filtered off, washed and dried. 16 parts of a product melting at 135 ° C. are obtained. That Filtrate contains about twice the amount of liquid high polymers, their lower boiling point is above 250 ° C at normal pressure. Example 2 100 parts of freshly distilled Styrene, 200 parts of cyclohexane, 5 parts of phenylbiphenyl ketone and 2 parts of potassium Stirred at 65 ° C under nitrogen for one hour. Then 0.5 part is passed Carbon tetrachloride. After one hour, the reaction mixture is cooled and slowly mixed with 1000 parts of methanol. The deposited polystyrene will filtered off, washed with methanolic hydrochloric acid and with methanol and dried. 70 parts of pale yellowish polystyrene are obtained.

Beispiel 3 In einem mit Stickstoff gespülten Schüttelautoklav wird eine Mischung aus 100 Teilen frisch destilliertem Vinylidenchlorid, 200 Teilen n-Hexan, 5 Teilen Phenylbiphenylketon, 2 Teilen Kalium und 0',5 Teilen Tetrachlorkohlenstoff 1 Stunde auf 100° C erhitzt. Man trennt das Polymerisat ab, reinigt es, wie im Beispiel 2 angegeben wurde, und erhält 80 Teile Polyvinvlidenchlorid.Example 3 In a shaking autoclave flushed with nitrogen a mixture of 100 parts of freshly distilled vinylidene chloride, 200 parts of n-hexane, 5 parts of phenyl biphenyl ketone, 2 parts of potassium and 0.5 parts of carbon tetrachloride Heated to 100 ° C for 1 hour. The polymer is separated off and cleaned as in the example 2 was given, and contains 80 parts of polyvinylidene chloride.

Claims (1)

PATE :iTANSPRL'CU: Verfahren zur Herstellung von Polymerisationsprodukten aus olefinisch-ungesättigten Verbindungen, dadurch gekennzeichnet, daß man Anlagerungsverbindungen von Metallen oder Gemischen aus Metallen und MetaIIhalogeniden an Ketone, gegebenenfalls unter Zusatz von Zn C12, A1 Cl", Fe C13, Si C14, Ti C14 oder Äthylchlorid, Chloroform, Tetrachlorkohlenstoff, Dichloräthan, Hexachloräthan, Trichlorbrommethan, Trifluorjodmethan, tert.-Butylchlorid, Triphenylchlorinethan, Trichloracetonitril oder Benzotrichlorid oder deren Gemischen, als Polymerisationskatalysatoren verwendet. PATE : iTANSPRL'CU: Process for the preparation of polymerization products from olefinically unsaturated compounds, characterized in that addition compounds of metals or mixtures of metals and metal halides with ketones, optionally with the addition of Zn C12, A1 Cl ", Fe C13, Si C14 , Ti C14 or ethyl chloride, chloroform, carbon tetrachloride, dichloroethane, hexachloroethane, trichlorobromomethane, trifluoroiodomethane, tert-butyl chloride, triphenylchlorinethane, trichloroacetonitrile or benzotrichloride or mixtures thereof are used as polymerization catalysts.
DEB35887A 1955-05-25 1955-05-25 Process for the preparation of polymerization products Pending DE1058257B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DEB35887A DE1058257B (en) 1955-05-25 1955-05-25 Process for the preparation of polymerization products

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEB35887A DE1058257B (en) 1955-05-25 1955-05-25 Process for the preparation of polymerization products

Publications (1)

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DE1058257B true DE1058257B (en) 1959-05-27

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1180522B (en) * 1962-08-25 1964-10-29 Basf Ag Process for the polymerisation of compounds with polymerisable CC double bonds
US3299118A (en) * 1963-08-12 1967-01-17 Shell Oil Co Production of epsilon-halonitriles by the 1, 4-addition of an alpha-halonitrile to aconjugated diene
DE1236198B (en) * 1962-04-21 1967-03-09 Basf Ag Process for the production of polymers from olefinically unsaturated hydrocarbons
DE1251954B (en) * 1963-06-11 1967-10-12 Basf Ag Process for the production of homo- or copolymers of ethylenically unsaturated hydrocarbons

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1236198B (en) * 1962-04-21 1967-03-09 Basf Ag Process for the production of polymers from olefinically unsaturated hydrocarbons
DE1180522B (en) * 1962-08-25 1964-10-29 Basf Ag Process for the polymerisation of compounds with polymerisable CC double bonds
DE1251954B (en) * 1963-06-11 1967-10-12 Basf Ag Process for the production of homo- or copolymers of ethylenically unsaturated hydrocarbons
US3299118A (en) * 1963-08-12 1967-01-17 Shell Oil Co Production of epsilon-halonitriles by the 1, 4-addition of an alpha-halonitrile to aconjugated diene

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