CA1296346C - Process for activation of titanium and vanadium catalysts useful in ethylene polymerization - Google Patents

Process for activation of titanium and vanadium catalysts useful in ethylene polymerization

Info

Publication number
CA1296346C
CA1296346C CA000590390A CA590390A CA1296346C CA 1296346 C CA1296346 C CA 1296346C CA 000590390 A CA000590390 A CA 000590390A CA 590390 A CA590390 A CA 590390A CA 1296346 C CA1296346 C CA 1296346C
Authority
CA
Canada
Prior art keywords
alkyl
carbon atoms
lewis acid
complex
electron donor
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.)
Expired - Lifetime
Application number
CA000590390A
Other languages
French (fr)
Inventor
Kevin J. Cann
Frederick J. Karol
David L. Miles
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.)
Union Carbide Corp
Original Assignee
Union Carbide Corp
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 claimed from US06/833,148 external-priority patent/US4670526A/en
Application filed by Union Carbide Corp filed Critical Union Carbide Corp
Application granted granted Critical
Publication of CA1296346C publication Critical patent/CA1296346C/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

ABSTRACT OF THE DISCLOSURE
The specification describes a complex consisting essentially of the reaction product of a divalent magnesium halide; a Lewis acid having the formula RmAlXn or RmBXn wherein R is an alkyl or aromatic radical, each radical having 1 to 12 carbon atoms and each R being alike or different; X is a halogen atom;
m is an integer from 0 to 3; n is an integer from 0 to 3; and m+n equals 3; and an electron donor compound selected from the group consisting of alkyl esters or alkyls and aromatic carboxylic acids and alkyl and cycloalkyl ethers, each compound having 2 to 12 carbon atoms. The complex is useful for activation of ethylene polymerization catalysts.

Description

i3 ~

COMPI.E~ USEE'[JL FOR ACTIVATION OF TITA~ M AND
VANADIUM CATALYSTS FOR El~IYLENE POLYME~I ZATION

This invention relates to a complex use~ul for the activation of an ethylene polymerization catalyst.
This application is a division of copending Canadian Patent Application Serial No. 530,090 filed February 19, 1987. The patent application is concerned with a process for activation of a titanium or vanadium compound using the complex of the present invention and the production of polyethylene from the activated compound.
A typical ethylene polymerization catalyst is prepared by forming a precursor from a magnesium compound, a titanium compound, and an electron donor compound; diluting the precursor with an inert carrier material; and activating the precursor by introducing an organoaluminum compound. The process is described in United States patents 4,302,565; 4,302,566; and 4,303,771. The magnesium and titanium compounds are dissolved in the electron donor compound (solvent) at a temperature ranging from ambient to below the boiling point of the electron donor. The order of addition to the electron donor compound is not important to the ~5 result, i.e., one or the other of the magnesium and titanium compounds can be added first or they can be added together. The dissolution in the electron donor compound can be enhanced by slurrying or refluxing.
After the magnesium and titanium compounds are dissolved, the resulting product is isolated by crystallization or precipitation with a hydrocarbon such as hexane, isopentane, or benzene. The cr~stallized or precipitated product is dried and recovered as fine, free-flowing particles. The magnesium/titanium based composition is then mixed with, or impregnated into, an `~k 3~;

inert carrier material. The carrier is generally a solid, particulate, porous material such as silica.
In order for the magnesium/titanium based composition to be useful as a polymerization catalyst, it must be activated with a compound capable of transforming the magnesium/titanium atoms to a state which will effect the desired polymerization reaction.
Activation is accomplished by the addition of an organoaluminum compound. Par~ial activation, if desired, is effected outside of the polymerization reactor by introducing the catalyst composition and the organoaluminum into a solvent. Complete activation is then carried out in the reactor as described in United States patent 4,383,095.
While the magnesium/titanium based catalyst compositions have proved to be satisfactory ethylene polymerization catalysts, there is a continuing effort to improve on the catalysis aspect of ethylene polymerization and, more particularly, to improve the technique for catalyst activation.
In accordance with the present invention, there is provided a complex consisting essentially of the reaction product of a diva]ent magnesium halide; a Lewis acid having the formula RmAlXn or RmBXn wherein R is an 2~ alkyl or aromatic radical, each radical having 1 to 12 carbon atoms and each R being alike or different; ~ is a halogen atom; m is an integer from 0 to 3; n is an integer from 0 to 3; and m+n equals 3; and an electron donor compound selected from the group consisting of alkyl esters of alkyl and aromatic carboxylic acids and alkyl and cycloalkyl ethers, each compound having 2 to 12 carbon atoms.
The novel complex of the present invention is useful for the activation of known ethylene polymerization catalysts, namely titanium or vanadium compounds, in simpler and more rapid manner than the - ~z~

prior art rou~e to activated magnesium/titanium based catalyst referred to above.
Titanium or vanadium compounds of interest here are commonly used as catalyst components in the polymerization of ethylene. Typical titanium compounds have the formula Ti(OR)nX4_n wherein R is a hydrocarbyl group having 1 to 14 carhon atoms or a COR' radical wherein R' is a hydrocarbyl group having 1 to 14 carbon atoms; X is a halide radical; and n is an integer from 0 to 4. Examples of titanium compounds are TiC14; TiBr4;
TiI4; Ti (OCH3) C13; Ti (OC6Hs) C13; Ti(OCOCH3)C13;
Ti (OCOC6Hs) C13; Ti (OC2H5) C13; Ti (OC2Hs) 2C12;
Ti(OC3H7)2C12; Ti(OC2H5)3C1; Ti(OC6H5)3Cl, Ti(oc2H5)4;
Ti(OC3H7)4; Ti(OC4Hg)~,; Ti(OC6H13)4~ Ti(C6Hll)4;
Ti(C8H17)4; Ti(ocH2 (c2H5) CHC4Hg)4; Ti(oc9Hl9)~
Ti[OC6H3(CH3)2]4; Ti(OCH3)2(OC4Hg)2; Ti(oc3H7)3(oc4Hs);
Ti(OC2H5)2(OC4Hg)2; Ti(OC2H4OCH3)4; and Ti(OC2H4C1)4.
Examples of vanadium compounds are VC14, VC13, VOC13, triisobutyl vanadate, and vanadium tris-acetyl acetonate. Other suitable vanadium compounds are mentioned in United States patents 3,956,255 and 4~370~455O
The complexes of the present invention contain these components, namely an electron donor compound, a divalent magnesium halide and a Lewis acid.
The electron donor solvents are organic compounds, liquid at temperatures in the range of about 0C to about 200C, in which the magnesium halide and defined Lewis acids are soluble. The electron donor solvents are also known as Lewis bases.
The electron donor compounds are selected from the group consisting of alkyl esters of alkyl and aromatic carboxylic acids and alkyl and cycloalkyl ethers, each compound having 2 to 12 carbon atoms. Among these electron donor compounds the preferable ones are alkyl esters of saturated alkyl carboxylic acids having l to 4 63~6 carbon atoms; alkyl esters of aromatic carboxylic acids having 7 or 8 carbon atoms; alkyl ethers having 2 to 8 carbon atoms, preferably 4 or 5 carbon atoms; and cycloalkyl ethers having 4 or 5 carbon atoms; preferably mono- or di-ethers having 4 carbon atoms. The most preferred oP these electron donor compounds include methyl formate, ethyl acetate, and butyl acetate, ethyl ether, tetrahydrofuran, and dioxane. Other examples of electron donor compounds are di-n-propyl ether, dibutyl ether, ethyl formate, methyl acetate, ethyl anisate, ethylene carbonate, tetrahydropyran, and ethyl propionate.
The divalent magnesium halide can be represented by the formula MgX2 wherein X is selected from the group consisting of Cl, Br and I.
Suitable magnesium compounds include MgC12, MgBr2 and MgI2. Anhydrous MgC12 is particularly preferred.
The Lewis acids are those having the formula RmAlXn or RmBXn wherein R is an alkyl or aromatic radical, each ~0 radical having 1 to 12 carbon atoms and each R being alike or different; X is a halogen atom; M is an integer from O to 3; n is an integer from 0 to 3; and m~n equals 3. Examples of alkyl radicals are: methyl, ethyl, propyl, isopropyl, butyl, isobutyl, tert-butyl, pentyl, ~5 neopentyl, hexyl, 2-methylpentyl, heptyl, octyl, isooctyl, 2-ethylhexyl, 5,5-dimethylhexyl, nonyl, decyl, isodecyl, undecyl, and dodecyl. Examples of aromatic radicals are: phenyl, phenethyl, methoxyphenyl, benzyl, tolyl, xylyl, naphthyl, naphthal, and methylnaphthyl.
Examples of halogens are chlorine, bromine and iodine.
Preferred Lewis acids are AlC13, C2~5AlC12, (C2H5)2A1C1, (C2Hs)3A1 and BC13. Other examples oP
suitable Lewis acids are triisobutyl aluminum, tributylaluminum, dibutyl-aluminum chloride, diethylalumlnum bromide, propyl-aluminum dichloride, butylaluminum dibromide, A1(C6H13)3~ Al(C8H17)3 - ~2~Çi3-~6 trimethylaluminum, diisobutylaluminum chloride, isobutylalumin~m dichloride, diethylaluminum methoxide, diethylaluminum ethoxide, dimethylaluminum chloride, and methylaluminum dichloride.
The magnesium halide/Lewis acid/electron donor complex, which may also be referred to as an adduct or solvated adduct, may be ~ormed by dissolving the divalent ma~nesium halide in an electron donor together with a Lewis acid at a temperature in the range of about 0C to about 200C. The molar ratio of magnesium halide to Lewis acid ~an be in the range of about 0.1 mole to about 4 moles of magnesium halide to one mole of Lewis acid and is preferably in the range of about 0.5 mole to about 2 moles of magnesium halide to one mole of Lewis acid. An excess of electron donor compound, i.e., a number o~ moles of electron donor compound at least about 15 times greater than the total number of moles of magnesium halide and Lewis Acid combined, provides a sufficient number of moles of electron donor to yield the complex. While atmospheric pressure is generally used, pressure is not considered a significant factor.
These solvated adducts can be isolated by evaporation of excess solvent or by slow crystallization of the adduct after partial concentration of the solvent. Preferred complexes are derived from MgC12 and the Lewis acids AlC13~ C2H5A1C12, (c2Hs)2Alcl~ (C2Hs)3Al, and BC13.
These complexes are as follows:
MgC12-2AlC13.nTHF MgC12~2AlC13,nEtoAC
MgC12-2EADC-nTHF MgC12~2BC13~6EtOAC
MgC12-EADC-nTHF MgC12~2EADC-nEtOAC
2MgC12~TEAL-nTHF
wherein n can be an integer from 1 to 13 and is preferably an integer from 5 to 12. The integer represents the number of moles of electron donor compound.

3~2~63-~6 The following acronyms are used above and ~hroughout this specification:
EADC = ethylaluminum dichloride THF = tetrahydrofuran TEAL = triethylaluminum EtOAC = ethyl acetate DEAC = diethylaluminum chloride Analyses of six of the complexes are set forth in Table I.
I TABLE
Analyzed Molar Analyses (weight %) Stoichiometries Complex _Ma Al B ~ A1 B
MgC12 2AlC13 nTHF 2.14 5.46 - 1 2.27 MgC12 2EADC nTHF 2.74 6.71 - 1 2.20 MgC12 EADC nTHF 4.44 5.25 - 1 1.06 2MgC12 TEAL nTHF 6.48 3.56 - 2.02 MgC12 2BC13 6EtOAC 3.01 - 2.79 1 - 2.04 MgC12 2EADC nEtOAC 2.42 5.57 - 1 2.07 The family of subject complexes is found to activate titanium or vanadium compounds, particularly titanium tetrachloride, in the presence of a hydrocarbyl aluminum compourld as a cocatalyst, in ~5 ethylene gas phase or slurred polymerization reactions. A catalyst, prepared by slurrying one of these complexes with titanium tetrachloride in hexane (or another inert hydrocarbon solvent), followed by washing with excess hexane and drying under reduced pressure possesses excellent activity in hexane polymerization reactions employing triethyl aluminum as a cocatalyst.
The hydrocarbyl aluminum cocatalyst can be represented by the formula R3Al wherein each R is an alkyl, cycloalls:yl, aryl, or hydride radical; at least one R is a hydrocarbyl radical; two or three R
radicaIs can be joined in a cyclic radical forming a heterocyclic ,~

i 3 ~ ~

structure; each R can be alike or different; and each R, which is a hydrocarbyl radical, has 1 to 20 carbon atoms, and preferably 1 to 10 carbon atoms. Further, each alkyl radical can be straight or branched chain and such hydrocarbyl radical can be a mixed radic~l, i.e., the radical can contain alkyl, aryl, and/or cycloalkyl groups. Examples of suitable radicals are: methyl, ethyl, propyl, isopropyl, bu~yl, isobutyl, tert-butyl, pentyl, neopentyl, hexyl, 2-methylpentyl, heptyl, octyl, isooctyl, 2-ethylhexyl, 5,5-dimethylhexyl, nonyl, decyl, isodecyl, undecyl, dodecyl, phenyl, phenethyl, methoxyphenyl, benzyl, tolyl, xylyl, naphthyl, naphthal, methylnaphthyl, cycohexyl, cycloheptyl, and cyclooctyl.
Examples of hydrocarbyl aluminum compounds are as follows: triisobutylaluminum, trihexylaluminum, di-isobutylaluminum, hydride, dihexylaluminum hydride, isobutylaluminum dihydride, hexylaluminum dihydride, di-isobutylhexylaluminum, isobutyl dihexylaluminum, trimethylaluminum, triethylaluminum, tripropylaluminum, triisopropylaluminum, tri-n-butylaluminum, trioctylaluminum, tridecylaluminum, tridodecylaluminum, t r ib e n z y l a lu m in u m, t r ip h e n y l al u m i n u m, trinaphthylaluminum, and tritolylaluminum. The preferred hydrocarbyl aluminums are triethylaluminum, triisobutylaluminum, trihexylaluminum, di-isobutylaluminum hydride, and dihexylaluminum hydride.
These comple~es also activate titanium or vanadium compounds when the complex is first impregnated on a silica support. The purpose o~ the impregnation is to produce polymers o~ preferred shape and bulk density.
To achieve this end, the magnesium halide and Lewis acid are dissolved in the electron donor solvent and slurried with the silica support. The excess solvent is then removed by purging or evaporation under reduced pressure. The resulting impregnated complexes are 3 ~

slurried with, for example, the tetravalent titanium compound in hexane, followsd by washing with excess hexane and drying, as above. These impregnated catalysts are also found to be active with triethyl aluminum as a cocatalyst. The result of the copolymerization is not only high catalyst activity, but high bulk density as well.
Further, it is ~ound that the solubility of the divalent magnesium halide is the electron donor solvent is increased by the presence of the defined Lewis acid, e.g., the degree of solubility of MgC12 in tetrahydrofuran is increased 100 percent by using a 0.6 molar solution of triethylaluminum in tetrahydrofuran.
Conductivity experiments measure the ability of a solution to carry a charge across a fixed path between two electrodes. If the bonding interaction between the magnesium halide and the Lewis acid in the electron donor solvent is ionic then a significant increase in conductivity over each component alone in the electron donor solvent should occur. The results of a series of conductivity experiments indicate just such an increase and it is therefore concluded that the subject complex is ionic in character. Since the conductive capacity is reached almost immediately upon mixing the components, there apparently is no kinetic barrier to interaction of the magnesium halide and Lewis acid in the electron donor solvent.
Impregnation of subject complex into, for example, silica prior to its use in titanium or vanadium compound activation is desirable to provide improved particle morphology. The impregnation is accomplished by mixiny the complex and silica gel in the electron donor solvent followed by solvent removal under reduced pressure.
Ethylene polymerization reactions are run by either slurrying the silica gel supported complex with the tetravalent titanium compound or isolating the 3~

impregnated silica gel after treatment with the tetravalen~ titanium compound, and then using the slurry or isolated precursor in the polymerization reaction.
It is found that the levels of catalyst activity, resin properties, and bulk densi~ies compare favorably with catalysts exemplified by the reaction product of m a g n e s i u m d i c h 1 o r i d e / t i t a n i u m tetrachloride/tetrahydrofuran and triethyl aluminum.
The invention is illustrated by the following examples:
Complexes are formed when magnesium dichloride and a defined Lewis acid are dissolved in an e~cess of electron donor solvent. The solvated complex is isolated by evaporation of excess solvent or slow crystallization after partial evaporation of the solvent. The complex is either (1) slurried with titanium tetrachloride in hexane to form a precursor, which is then isolated, or (2) slurried with titanium tetrachloride in hexane just prior to introduction into the polymerization reactor.

Example 1 The complex MgC12/2EADC/THF is prepared as follows:
to a flask is added 1.93 grams (15 millimoles) of ethylaluminum dichloride. After chilling to ODC, one cubic centimeter of THF is added and the solid dissolves immediately. After warming to room temperature, 9 cubic centimeters of 0.51 molar MgC12 in THF is added and a white precipitate forms immediately. The mixture is warmed to 40C and all of the solid dissolves. Upon cooling to ambient temperature, the precipitate reforms.
The mixture is cooled to 0C and the mother liquor is decanted away. The residue is then washed with cold THF
and dried under high vacuum.
Analysis of complex:
6.71% by weight aluminum ;3 ~

2.74% by weight magnesium Proton nuclear magnetic resonance (CH2C12, chemical shift in parts per million): minus 0.15 quartet; 0.83 triplet; 1.80 multiplet, 3.90 multiplet. This spectrum is uniquely different from any of the starting materials.

Exam~le 2 The complex MgC12/EADC/THF is prepared as follows:
to a flask is added 1.94 grams (15 millimoles) of ethyl aluminum dichloride. Af~er cooling the flask to 0~C, 13.3 cubic centimeters of 0.52 molar MgC12 (6.9 millimoles) in THF is added. The solution is concentrated to 5 cubic centimeters and a crop of crystals is collected by decanting away the mother liquor. The mother liquor is allowed to stand and a second crop of crystals is collected.
Analysis of complex (second crop of crystals):
5.256 by weight aluminum 4.44% by weight magnesium Infrared spectrum (Nujol* mull; cm~1), ether absorptions only: 1025; 1015; 875; 862; 848. As in example 1, this spectrum is uniquely different from any of the starting materials.
Example 3 The complex MgC12/2EADC/EtOAC is prepared as follows: to a flask is added 1.9 grams (15 millimoles) of ethyl aluminum dichloride with 8 cubic centimeters of 0.52 molar MgC12 in EtOAC. A precipitate forms immediately. The mixture is warmed and allowed to cool slowly. A~ white solid forms and is aollected by decanting away the mother liquor. The remaining solid is cooled and washed two times with cold EtOAC.
* Trademark ~2~3.~6~

Analysis:
2.42~ by weight magnesium 5.57% by weight aluminum HlNMR (nuclear magnetic resonance) spectrum (CH2C12, chemical shift in parts per million): minus 0.05 quartet; 0.95 triplet; 1.17 triplet; 2.14 singlet;
4.14 quartet.
This spectrum is also uniquely different from any of the starting materials.
Example 4 The complex MgC12/2 BC13/EtOAC is prepared as follows: to a flask are added equal volumes of 0.13 molar MgC12 and BC13 solutions in ethyl acetate. A
white precipitate forms immediately and is isolated by filtration.
Analysis:
3.01% by weight magnesium 2.79% by weight boron 34.7% by weight chlorine Examples 5 to 8 The catalyst in examples 5 to 8 is prepared by isolating an adduct forméd by slurrying the complex with ~5 an excess of TiC14 in hexane. The titanium derivative is isolated by decanting away the hexane solution and washing the residue with excess hexane. Additional steps, conditions, and results will be found below and in Table II.
Example 9 The complex is slurried with 7 milligrams of TiC14 just prior to addition to the polymerization reaction.
Additional steps, conditions, and results will be found below and in Table II.

~ ~9~3 ~i Examples 10 and ll (a) To a flask is added 12.67 grams of silica, which has been dried under a ni~rogen purge at 800C.
To the silica is added 75 cubic centimeters of THF
followed by 5.9 cubic centimeters of 1.5 molar EADC in hexane (8.85 millimoles). Next, 8.5 cubic centimeters of 0.52 molar MgC12 in THF is added. After stirring, the solvent is removed under reduced pressure.
(b) To a flask is charged 5.48 grams of the supported complex with 20 cu~ic centimeters of hexane.
To this is added 0.35 millimoles of TiC14 per gram of supported complex. The mixutre is stirred, allowed to settle, and the solvent is decanted away. The solid is washed three times with hexane, then dried under vacuum.
Additional steps, conditions, and results will be found below in Table II.

Examples 12 and 13 Example lO is repeated except that D~AC is substituted for EADC. Additional steps, conditions, and results will be found below and in Table II.
Each catalyst of examples 5 to 13 and TEAL as a cocatalyst are added to a reaction vessel containing 20 cubic centimeters of l-hexane. Ethylene is introduced at an initial pressure of 0.89 megaPascal. Hydrogen is also introduced at 0.14 megaPascal. The reaction temperature is 85C.
Table II sets forth the following conditions and results:
1. The isolated magnesium halide/Lewis acid~electron donor complex. Milligrams of catalyst are set forth in parentheses. In examples 10 to 13, this weight includes the support.
2. The method of titanium addition, i.e., (1) or (2) described above. In method (2), the milligrams of 6~

titanium added in examples 9, 11, and 13 are 7, 6.9, and .9, respectively.
3. The percentage of titanium in the catalyst.
4. Triethylaluminum is used as a cocatalyst. The mole ratio of triethylaluminum to titanium is given.
5. The activity of the catalyst in kilograms of polyethylene per millimole of titanium per hour at an ethylene pressure of one megaPascal.
6. Melt index: ASTM D-1238, Condition E.
Measured at 190C and reported as grams per 10 minutes.
7. Melt flow ratio: Ratio of Flow Index to Melt Index. Flow index: ASTM D-1238, Condition F. Measured at 10 times the weight used in the melt index text above.
8. Polymer density: ASTM D-1505 procedure is followed for polymers having a density of less than 0.940 grams per cubic centimeter and a modified procedure is used for polymers having a density equal to or greater than 0.940 grams per cubic centimeter. For the low density polymers, a plaque is made and conditioned for one hour at 100C to approach equilibrium crystallinity. For the high density polymers, the plaque is conditioned for one hour at 120DC to approach equilibrium crystallinity, and is then quickly cooled to room temperature. Measurement for density is then made in a density gradient column and density values are reported as grams per cubic centimeter.
9. Polymer bulk density: ASTM D-1895, Method B.
The resin is poured via a 3/8 inch diamter funnel into a 400 milliliter graduated cylinder to the 400 milliliter line without shaking the cylinder, and weighed by difference. Density values are reported as kilograms per cubic meter.

.

3'~ `
._, '1. 'I

~ ~ ~ ~ I I I I I o o o o o ~ 3~ ~

u~ c~ ~ 3 o~ ul o ao 4 U ~ ~ ~ ~ ,~
O ~ ~ID
P-a o o o o I o o o o .~ ~ ~ I
_I O ~ ~ I ~ I ~ U~

E ~ ~ I I ~ ~

P,~ ~ o~ o o C`l o~
~ ~ 0 U~ o~ o o~
1 ~3 E
_ _ ~: ~.C

~o ooooooooo ~0 ~ ~ ~ ~ ~ ~ ~ d` 3 t~:l E~
'1:
o r~
u~X x c~
C ~ ~ 3 ~ I _ h ~
P~
C
O
O r~ ~- 1~
o ~S

~ o~
r~
O ~ ~ ~`
O CO
O ~0 o ~
8 ~ . . ~ ~ ~ ~ ~ ~

.
~ ,, , _, ' . ' '.:

Claims

The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:
1. A complex consisting essentially of the reaction product of a divalent magnesium halide; a Lewis acid having the formula RmAlXn or RmBXn wherein R is an alkyl or aromatic radical, each radical having 1 to 12 carbon atoms and each R being alike or different;
X is a halogen atom; m is an integer from 0 to 3; n is an integer from 0 to 3; and m+n equals 3; and an electron donor compound selected from the group consisting of alkyl esters of alkyl and aromatic carboxylic acids and alkyl and cycloalkyl ethers, each compound having 2 to 12 carbon atoms wherein the ratio of magnesium halide to Lewis acid is in the range of about 0.1 mole to about 4 moles of magnesium halide per mole of Lewis acid, said reaction product being formed on dissolution of magnesium halide and Lewis acid in the electron donor compound.
2. The complex defined in claim 1 wherein the halide is divalent magnesium chloride.
3. The complex defined in claim 1 wherein the Lewis acid is selected from the group consisting of AlCl3, C2H5AlCl2, (C2H5)2AlCl, (C2H5)3Al, and BCl3.
4. The complex defined in claim 3 wherein the electron donor compound is selected from the group consisting of alkyl esters of saturated alkyl carboxylic acids having 1 to 4 carbon atoms; alkyl esters of aromatic carboxylic acids having 7 or 8 carbon atoms; alkyl ethers having 2 to 8 carbon atoms; and cycloalkyl ethers having 4 or 5 carbon atoms.

5. The complex defined in claim 4 wherein the electron donor compound is selected from the group consisting of methyl formate, ethyl acetate, butyl acetate, ethyl ether, tetrahydrofuran, and dioxane.
6. The complex defined in claim 5 wherein the ratio of magnesium halide to Lewis acid is in the range of about 0.5 mole to about 2 moles of magnesium halide per mole of Lewis acid.
CA000590390A 1986-02-27 1989-02-07 Process for activation of titanium and vanadium catalysts useful in ethylene polymerization Expired - Lifetime CA1296346C (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US06/833,148 US4670526A (en) 1986-02-27 1986-02-27 Process for activation of titanium and vanadium catalysts useful in ethylene polymerization
US833,148 1986-02-27
CA000530090A CA1269197A (en) 1986-02-27 1987-02-19 Process for activation of titanium and vanadium catalysts useful in ethylene polymerization

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
CA000530090A Division CA1269197A (en) 1986-02-27 1987-02-19 Process for activation of titanium and vanadium catalysts useful in ethylene polymerization

Publications (1)

Publication Number Publication Date
CA1296346C true CA1296346C (en) 1992-02-25

Family

ID=25671239

Family Applications (1)

Application Number Title Priority Date Filing Date
CA000590390A Expired - Lifetime CA1296346C (en) 1986-02-27 1989-02-07 Process for activation of titanium and vanadium catalysts useful in ethylene polymerization

Country Status (1)

Country Link
CA (1) CA1296346C (en)

Similar Documents

Publication Publication Date Title
EP0314165B1 (en) Process for the production of polyethylene with a broad and/or bimodal molecular weight distribution
US4755495A (en) Process for activation of titanium and vanadium catalysts useful in ethylene polymerization
CA1187470A (en) Solid catalyst component for olefin polymerization
JPS61130312A (en) Production of catalyst component for olefin polymerization
US4151337A (en) Process for preparing polyolefin
SK278631B6 (en) The solid catalyst on the titanium chloride base, applicable to the stereospecific polymerisation of alpha-oleins and preparation method thereof
US4426317A (en) Process for making olefin polymerization catalyst
EP1511780B1 (en) Ziegler natta catalyst components for the polymerization of olefins
US4738942A (en) Catalyst composition for polymerizing alpha-olefin polymers of relatively narrow molecular weight distribution and high melt index
KR920004806B1 (en) Process for simultanously dimerizing ethylene and copolymerizing ethylene with the dimerized product
US3773735A (en) Process for the manufacture of polyolefins
US4357452A (en) Process for polymerizing propylene
US4622309A (en) Novel titanium complexes and catalysts prepared therefrom
CA1269197A (en) Process for activation of titanium and vanadium catalysts useful in ethylene polymerization
CA1296346C (en) Process for activation of titanium and vanadium catalysts useful in ethylene polymerization
JPH0415807B2 (en)
EP0286001B1 (en) Process for the production of polyethylene having an intermediate molecular weight distribution
KR920004424B1 (en) Ethylene polymerization catalyst
US4354959A (en) Catalyst for polymerizing olefins
CA1216274A (en) Solid catalyst component for olefin polymerization
JPS5812889B2 (en) Polyethylene material
JPS6225112A (en) Production of ethylenic copolymer
JP2677394B2 (en) Method for producing magnesium chloride-supported titanium catalyst
JPS61207405A (en) Polymerization of ethylene
US4885349A (en) Process for polymerizing alpha-olefin polymers of relatively narrow molecular weight distribution and high melt index

Legal Events

Date Code Title Description
MKLA Lapsed