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公开(公告)号:DE3144312A1
公开(公告)日:1983-05-19
申请号:DE3144312
申请日:1981-11-07
Applicant: BASF AG
Inventor: JAGGARD JAMES F R DIPL CHEM DR , SCHWEIER GUENTHER DIPL CHEM DR , KLAERNER PETER DIPL CHEM DR
IPC: C08F297/08 , C08F293/00
Abstract: Propylene/ethylene block copolymers are prepared by a process in which, in an agitated bed comprising small polymer particles, first (I) propylene is homopolymerized from the gas phase, in a first polymerization zone, by feeding in a Ziegler-Natta catalyst comprising (1) a titanium(III) component and (2) a dialkyl-aluminum chloride component, with or without (3) a further catalyst component, and then (II) the product obtained in the first polymerization zone is fed into a second polymerization zone, where a mixture of propylene and ethylene is polymerized with the propylene homopolymer present in this product. In this process, the Ziegler-Natta catalyst employed contains a titanium(III) component (1) which is prepared by subjecting (1.1) a titanium-containing compound (a) of the formula TiCl3. nAlCl3 and (1.2) an electron donor (b), consisting of (b1) an ester of a particular class or (b2) a phosphorus-containing compound of a particular class, to a special milling procedure, the particular features of which are special metering and temperature conditions, suspending the resulting intermediate in a mixture of a liquid hydrocarbon (c) and an oxygen-containing compound (d), comprising (d1) an ether of a certain class and/or (d2) an ester of a certain class, and then heating the suspension obtained. The solid remaining in suspension is the titanium(III) component (1) which is to be employed for the polymerization. The polymer obtained has improved morphological properties.
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公开(公告)号:DE3021296A1
公开(公告)日:1982-01-07
申请号:DE3021296
申请日:1980-06-06
Applicant: BASF AG
Inventor: JAGGARD JAMES F R DIPL CHEM DR , KLAERNER PETER DIPL CHEM DR , STAIGER GERHARD DIPL CHEM DR
Abstract: In the prepn. of a new Ti(III)-component (1) for Ziegler-Natta catalyst systems, a Ti-contg. cpd. having TiCl3.nAlCl3, (A), (where n is 0.01-1) is ground with a P-contg. cpd. having formula OmP(R1)3, (B), (where m is 0 or 1 ; R1 is R2, OR2 or N(R2)2 and R2 is 1-24C alkyl, aryl, alkaryl or aralkyl). Specific grinding conditions are used. (B) is added to (A) in quantities corresponding to molar ratio Ti in (A) : (B) 1 : 0.01 to 1 : 1. A suspension of (i) 1 pt.wt. of prod.; (ii) 0.5-20 pts.wt. hydrocarbon, (C), liq. under normal conditions and boiling below 150 deg.C; and (iii) an O-contg. cpd. (D) is prepd. (D) can be a 4-30C ether of formula R8-O-R8' (where R8 and R8' are 1-15C alkyl, Ph or 7-14C alkyl-phenyl) and/or a 2-34C ester having formula R9'-O-CO-R9 or R9'-O-CO-CR9=CHR9 (where R9 is H, 1-12C alkyl, 7-14C phenyl-alkyl in which Ph is opt. mono-alkyl substd., Ph or 7-14C alkyl-phenyl ; R9' is 1-8C alkyl, Ph or 7-14C phenyl-alkyl). (D)-quantities are such that molar ratio Ti in (A) to (D) is 1 : 0.01 to 1 : 2. The suspension is strongly stirred 5-120 min. at 40-140 deg. C and cooled to 15-25 deg.C. The solid separated from the suspension is opt. washed with a hydrocarbon, liq. under normal conditions and boiling below 150 deg.C and dried to recover the new Ti(III)-componentt (1). The catalyst systems are used in 2-6C alpha-mono-olefin (co)polymerisation. Stereoregular polymers are obtd. in high yields. The prods. have a low fine grain proportion.
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公开(公告)号:DE3021297A1
公开(公告)日:1982-01-07
申请号:DE3021297
申请日:1980-06-06
Applicant: BASF AG
Inventor: JAGGARD JAMES F R DIPL CHEM DR , KLAERNER PETER DIPL CHEM DR , STAIGER GERHARD DIPL CHEM DR
Abstract: In the prepn. of a new Ti(III)-component, (1), for Ziegler-Natta catalyst systems, a Ti-contg. cpd., (A), having formula TiCl3.nAlCl3 (where n is 0.01-1) is ground with a 2-34C ester, (B), having formula R1-O-CO-R2 or R1-O-CO-CR2=CHR2 (where R1 is 1-16C alkyl or 7-23C phenyl-alkyl in which the Ph gp. is opt. substd. by up to 5 1-4C alkyl gps.; R2 is H, 1-18C alkyl, 7-23C phenyl- alkyl or 7-23C alkyl-phenyl in which Pb is opt. substd. by up to 5 1-4C alkyl gps.). Specific grinding conditions are used. (B) is added to (A) in quantities corresponding to molar ratio Ti in (A) : (B) 1 : 1.5 to 1 : 0.01. A suspension of (i) 1 pt.wt. prod.; (ii) 0.5-20 pts.wt. hydrocarbon, (C), liq. under normal conditions and boiling below 150 deg.C; and (iii) a 1-20C alcohol, (D), having formula X(OH)y (where y is 1 or 2 and X is an aromatic, satd. aliphatic or cycloaliphatic hydrocarbyl gp.) is prepd. D-quantity is such as to set up molar ratio Ti in (A) : (D) 1 : 0.01 to 1 : 2. The suspension is then strongly stirred 5-120 min. at 40-140 deg.C and then cooled to 15-25 deg.C. The suspension is opt. mixed with an Al-contg cpd. (E) having formula Al(R8)x(Y)3-x (where x is 1-3; Y is Cl or R8; R8 is 1-12C alkyl). Quantities are such as to set up molar ratio OH gps. from (D) : alkyl gps. in (E) 1 : 0.005 to 1 : 2. The solid sepd. from the suspension is opt. washed with a hydrocarbon, liq. under normal conditions and boiling below 150 deg.C, and dried, to recover (I). The catalyst systems are used in 2-6C alpha-mono-olefin (co)polymerisation. Stereoregular polymers are obtd. in high yields. Fine grain proportion is reduced.
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公开(公告)号:DE3020870A1
公开(公告)日:1981-12-17
申请号:DE3020870
申请日:1980-06-02
Applicant: BASF AG
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公开(公告)号:DE3020827A1
公开(公告)日:1981-12-17
申请号:DE3020827
申请日:1980-06-02
Applicant: BASF AG
Inventor: JAGGARD JAMES F R DIPL CHEM DR , KLAERNER PETER DIPL CHEM DR , SCHWEIER GUENTHER DIPL CHEM DR
Abstract: Alpha-olefins are polymerized with a catalyst containing (1) TiCl3/AlCl3 and (2) aluminum dialkyl chloride wherein (1) is prepared by milling the TiCl3/AlCl3 with a particular phosphorous compound under special conditions and then treating with a liquid hydrocarbon and an ether and/or ester.
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公开(公告)号:DE3130304A1
公开(公告)日:1983-02-17
申请号:DE3130304
申请日:1981-07-31
Applicant: BASF AG
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公开(公告)号:DE3018113A1
公开(公告)日:1981-11-19
申请号:DE3018113
申请日:1980-05-12
Applicant: BASF AG
Inventor: JAGGARD JAMES F R DIPL CHEM DR , KLAERNER PETER DIPL CHEM DR , SCHWEIER GUENTHER DIPL CHEM DR
Abstract: A process for the preparation of homopolymers and copolymers of alpha -monoolefins by means of a Ziegler-Natta catalyst system comprising (1) a titanium-III component, which is prepared by subjecting (1.1) a titanium trichloride/aluminum trichloride compound (a) and (1.2) an ester (b) to a certain type of milling treatment in which (A) a vibratory ball mill providing a relatively high milling acceleration is used, (B) the mill is first charged with the titanium-containing compound (a) and, if appropriate, is run for a certain period, thereafter (C) the ester (b) is added at a certain rate while milling the charge, thereupon (D) the charge is kept at +15 DEG C. or above for a certain period, while continuing the milling, hereupon (E), if appropriate, the product obtained from (D) is milled further for a certain period at +5 DEG C. or below, then (F), if appropriate, but advantageously so, the product obtained from (D) or (E) is kept at +20 DEG C. or above for a certain period, without milling, and thereafter (G), if appropriate, the product obtained from (F) is milled further for a certain period at +5 DEG C. or below, (2) an aluminum-alkyl component containing a chlorine bonded to the aluminum, and (3), if appropriate, a phenolic compound of a certain category, in which process a titanium-III component (1) is employed, in the preparation of which additionally -(H) a suspension is prepared from (H1) the product obtained according to (D), (E), (F) or (G), (H2) a liquid hydrocarbon (c) and (H3) an oxygen-containing compound (d), consisting of (d1) an ether of a certain category and/or (d2) an ester of a certain category, thereafter (I) the suspension obtained according to (H) is kept at an elevated temperature for a certain period, with vigorous agitation, and is then cooled, hereupon (J), if appropriate, the solid is isolated from the suspension obtained according to (I), and, if desired, is washed with a liquid hydrocarbon and dried, the novel titanium-III component (1) being the solid, in suspended form, obtained according to (I) or the solid, in isolated form, obtained according to (J). Using this Ziegler-Natta catalyst system, polymers with relatively high stereo-regularity and advantageous morphological properties can be obtained in relatively high yield.
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公开(公告)号:DE2841646A1
公开(公告)日:1980-04-03
申请号:DE2841646
申请日:1978-09-25
Applicant: BASF AG
Inventor: JAGGARD JAMES F R DIPL CHEM DR , HENNENBERGER PETER DIPL CHEM D , STAIGER GERHARD DIPL CHEM DR , KLAERNER PETER DIPL CHEM DR
Abstract: The process involves stopping and restarting the homo- or co-polymerisation 2-6C alpha-monoolefins at 40-120 degrees C. and 1-100 bar using a Ziegler-Natta catalyst of (a) a TiCl3 cocrystallisate of the formula TiCl3.nAlCl3 (in which n = 0.31-0.35), opt. modified with an electron donor, and (b) an Al cpd. of the formula R2AlX (in which R is 1-6C alkyl; X is Cl or R) in an (a):(b) molar ratio of 1:1-100. Polymerisation is stopped by introducing CO and/or CO2 to a concn. of min. 0.5 mmole/l. reactor vol. under 2 min. and restarted by replacing the CO/CO2 with fresh monomer. Overheating and the danger of explosion can be avoided easily and economically. Introduction of the stopper can be controlled automatically by a safety system.
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公开(公告)号:DE2519582A1
公开(公告)日:1976-11-18
申请号:DE2519582
申请日:1975-05-02
Applicant: BASF AG
Inventor: NICKL JOHANN DIPL CHEM DR , SCHICK HANS DIPL CHEM DR , MUELLER-TAMM HEINZ DIPL CHEM D , JAGGARD JAMES F R DIPL CHEM DR
Abstract: In the prepn. of a modified Ti congt. component of a Ziegler catalyst for the polymerisation of 3-6C monoolefins by dry grinding in a vibratory ball mill (a) a Ti cpd. of formula tiCl3. nAlCl3 (n = 0 to 0.7) and (b) a P cpd. of formula OmPX3 in which m = O or 1, X = R, OR or NR2 and R is alkyl-, aryl, -alkaryl- or aralkyl with 24C using molar ratio of (a):(b) = 1:0.01 to 1:1, mill acceleration = 30 to80 m.sec.-2, the improvement comprises reacting the dry ground product in the absence of thinning agents and without grinding and in intimate contact with 0.05-100 times its wt. of an Al cpd. of formula (Alk)2 AlY at 0-125, pref. 55-70 degrees C. for 0.1-100 hr. (where alk is 1-12C alkyl, Y = Cl or Br esp. Cl). The resulting solid is isolated, washed with an inert organic solvent and dried.
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