AU7122081A - Catalytic polymerisation of olefins - Google Patents

Catalytic polymerisation of olefins

Info

Publication number
AU7122081A
AU7122081A AU71220/81A AU7122081A AU7122081A AU 7122081 A AU7122081 A AU 7122081A AU 71220/81 A AU71220/81 A AU 71220/81A AU 7122081 A AU7122081 A AU 7122081A AU 7122081 A AU7122081 A AU 7122081A
Authority
AU
Australia
Prior art keywords
alkyl
carbon atoms
titanium
degrees
containing compound
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.)
Granted
Application number
AU71220/81A
Other versions
AU546919B2 (en
Inventor
James F.R. Jaggard
Peter Klaerner
Guenther Schweier
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
Publication of AU7122081A publication Critical patent/AU7122081A/en
Application granted granted Critical
Publication of AU546919B2 publication Critical patent/AU546919B2/en
Anticipated expiration legal-status Critical
Ceased 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)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Detergent Compositions (AREA)
  • Cosmetics (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

1. A process for the preparation of homopolymers and copolymers of C2 -alpha-monoolefins, at from 20 to 160 degrees C, under a pressure of from 1 to 100 bar, by means of a Ziegler-Natta catalyst system comprising (1) a titanium-III component, in the preparation of which (1.1) a titanium-containing compound (a) of the formula TiCl3 .nAlCl3 , where n is a number from 0.01 to 1, and (1.2) an ester (b), which contains a total of from 2 to 34 carbon atoms and has the formula R**1 -O-CO-R**2 or see diagramm : EP0041139,P12,F2 where R**1 is (I) alkyl of 1 to 16 carbon atoms or (II) phenylalkyl of a total of 7 to 23 carbon atoms, in which up to 5 hydrogen atoms of the phenyl radical can be substituted by alkyl of 1 to 4 carbon atoms, and R**2 is (I) hydrogen, (II) alkyl of 1 to 18 carbon atoms, (III) phenylalkyl of a total of 7 to 23 carbon atoms, in which up to 5 hydrogen atoms of the phenyl radical can be substituted by alkyl having 1 to 4 carbon atoms, (IV) phenyl or (V) alkylphenyl of a total of 7 to 23 carbon atoms, in which up to 5 hydrogen atoms of the phenyl radical can be substituted by alkyl of 1 to 4 carbon atoms, are subjected to a milling treatment, wherein (A) a vibratory ball mill having a milling acceleration of from 30 to 80 m . sec**-2 is used, (B) the mill is first charged with the titanium-containing compound (a) and - if desired - is run at from -50 to +100 degrees C for a period of from 0.5 to 100 hours in the absence of a diluent, thereafter (C) the amount of the ester (b) which corresponds to a molar ratio of titanium in the titanium-containing compound (a) : ester (b) of from 1:1.5 to 1:0.01 is added at a rate of 0.01-200 ml/min per 2.5 kg of titanium-containing compound (a), continuously or in small portions, and in the absence of a diluent, whilst milling the mixture at from -50 to +80 degrees C, thereupon (D) the material is kept for a period of from 1 to 120 hours at from +15 to +100 degrees C whilst being milled, following this (E) - if desired - the product obtained from (D) is milled further for a period of from 0.5 to 60 minutes at from -50 to +5 degrees C in the absence of a diluent, then (F) - if desired, and advantageously - the product obtained from (D) or (E) is kept for a period of from 0.25 to 300 hours at from +20 to +150 degrees C without being milled, and thereafter (G) - if desired - the product obtained from (F) is milled again, for a period of from 0.5 to 60 minutes, at from -50 to +5% C, in the absence of a diluent, (2) an aluminium-alkyl component of the formula see diagramm : EP0041139,P12,F1 where R**3 and R**4 are identical or different and each is alkyl of 1 to 8 carbon atoms, and (3) - if desired - a phenolic compound of the formula see diagramm : EP0041139,P12,F3 or see diagramm : EP0041139,P12,F4 where R**5 is C1 -C6 -alkyl, R**6 is hydrogen or C1 -C6 -alkyl, R**7 is hydrogen or a saturated hydrocarbon radical of not more than 30 carbon atoms, which may or may not contain up to a total of 6 ether groups and/or ester groups, R**7 ' is C2 -C24 -alkyl and o is an integer from 1 to 6, with the proviso that the atomic ratio of titanium from the titanium-III component (1) : aluminium from the aluminium-alkyl component (2) is from 1:1 to 1:20 and that, where relevant, the molar ratio of aluminium-alkyl component (2) : phenolic compound (3) is from 1:1 to 40:1, in which process a titanium-III component (1) is employed which has been prepared in the following manner : - (H) a suspension is prepared from (H1 ) 1 part by weight of the product obtained according to (D), (E), (F) or (G), (H2 ) from 0.5 to 20 parts by weight of a hydrocarbon (c) which is liquid under standard conditions of temperature and pressure and boils below 150 degrees C, and (H3 ) an oxygen-containing compound (d), consisting of an alcohol of 1 to 20 carbon atoms, which has the general formula X(OH)y where y is 1 or 2 and X is the radical of an aromatic or saturated aliphatic or cycloaliphatic hydrocarbon, in such as amount that the molar ratio of titanium from the titanium-containing compound (a) : oxygen-containing compound (d) is from 1:0.01 to 1:2, thereafter (I) the suspension obtained according to (H) is kept at from +40 to +140 degrees C for a period of from 5 to 120 minutes, with vigorous agitation, and is then brought to from +15 degrees C to +25 degrees C, thereupon (J) - if desired - the suspension obtained according to (I) is mixed with an aluminium-containing compound (e) of the general formula AIRx-8 Y3-x , where x is 1, 2 or 3, Y is chlorine or R**8 , and the R**8 's are identical or different alkyl groups of 1 to 12 carbon atoms, in such as amount that the molar ratio of hydroxyl groups of the oxygen-containing compound (d) : alkyl groups of the aluminium-containing compound (e) is from 1:0.005 to 1:2, and finally, (K) - if desired - the solid is isolated from the suspension obtained according to (I) or (J), if desired, washed with a hydrocarbon which is liquid under standard conditions of temperature and pressure and boils below 150 degrees C and dried, the solid in suspension obtained according to (I) or (J), or the isolated solid obtained according to (K), constituting the novel titanium-III component (1).
AU71220/81A 1980-06-02 1981-06-01 Catalytic polymerisation of olefins Ceased AU546919B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19803020870 DE3020870A1 (en) 1980-06-02 1980-06-02 METHOD FOR PRODUCING HOMO AND COPOLYMERISATES FROM (ALPHA) MONOOLEFINES BY MEANS OF A ZIEGLER-NATTA CATALYST SYSTEM
DE30208709 1980-06-02

Publications (2)

Publication Number Publication Date
AU7122081A true AU7122081A (en) 1981-12-10
AU546919B2 AU546919B2 (en) 1985-09-26

Family

ID=6103756

Family Applications (1)

Application Number Title Priority Date Filing Date
AU71220/81A Ceased AU546919B2 (en) 1980-06-02 1981-06-01 Catalytic polymerisation of olefins

Country Status (4)

Country Link
EP (1) EP0041139B1 (en)
AT (1) ATE3718T1 (en)
AU (1) AU546919B2 (en)
DE (2) DE3020870A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU567751B2 (en) * 1983-07-30 1987-12-03 Basf Aktiengesellschaft Catalytic polymerisation of olefins

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110016095B (en) * 2018-01-10 2021-07-02 中国石油化工股份有限公司 Solid catalyst component for olefin polymerization, preparation method thereof, catalyst and application thereof
CN110016096B (en) * 2018-01-10 2021-05-11 中国石油化工股份有限公司 Catalyst carrier for olefin polymerization and preparation method thereof, solid catalyst component, catalyst system and olefin polymerization method

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3850899A (en) * 1970-06-15 1974-11-26 Mitsui Petrochemical Ind Process for polymerizing olefins and catalyst therefor
DE2658939A1 (en) * 1976-12-24 1978-07-06 Basf Ag PROCESS FOR PRODUCING A TITANIUM CONTAINING COMPONENT FOR CATALYSTS OF THE ZIEGLER NATTA TYPE
DE2841645A1 (en) * 1978-09-25 1980-04-03 Basf Ag METHOD FOR PRODUCING HOMO AND COPOLYMERISATS FROM ALPHA MONOOLEFINES

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU567751B2 (en) * 1983-07-30 1987-12-03 Basf Aktiengesellschaft Catalytic polymerisation of olefins

Also Published As

Publication number Publication date
AU546919B2 (en) 1985-09-26
EP0041139A1 (en) 1981-12-09
EP0041139B1 (en) 1983-06-08
DE3160412D1 (en) 1983-07-14
ATE3718T1 (en) 1983-06-15
DE3020870A1 (en) 1981-12-17

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