Claims Analysis
Total Claims: 20
Claim 1
Independent Claim
220 words
A process for the production of a catalyst component for use in the polymerization of α-olefins which comprises reducing titanium tetrachloride at a temperature of from -50° to +30° C. with an organoaluminum compound or mixture of such compounds having the general formula A1R n X 3-n wherein R represents a hydrocarbon group having 1 to 18 carbon atoms, X represents a halogen atom and n represents a number expressed as 0<n≦3, to obtain a brown or black-brown titanium trichloride reduced solid containing aluminum compounds, removing aluminum compounds contained in said reduced solid, and thereafter contacting said reduced solid in an inert diluent and at a temperature within the range of from -30° to 100° C. for at least 30 minutes with an activator which is a complex or mixture of titanium tetrachloride and a dialkyl ether wherein the mole ratio of dialkyl ether to titanium tetrachloride is at least 0.1 and the concentration of titanium tetrachloride is maintained at at least 1 volume percent of the liquid phase, said dialkyl ether having the formula R'OR", in which R' and R" are the same or different and each are selected from the group consisting of (a) alkyl groups having 1 to 4 carbon atoms, (b) normal alkyl groups having 5 carbon atoms, and (c) alkyl groups having 6-20 carbon atoms.
Claim 2
Dependent Claim
220 words
A process for the production of a catalyst component for use in the polymerization of α-olefins which comprises reducing titanium tetrachloride at a temperature of from -50° to +30° C. with an organoaluminum compound or mixture of such compounds having the general formula A1R n X 3-n wherein R represents a hydrocarbon group having 1 to 18 carbon atoms, X represents a halogen atom and n represents a number expressed as 0<n≦3, to obtain a brown or black-brown titanium trichloride reduced solid containing aluminum compounds, removing aluminum compounds contained in said reduced solid, and thereafter contacting said reduced solid in an inert diluent and at a temperature within the range of from -30° to 100° C. for at least 30 minutes with an activator which is a complex or mixture of titanium tetrachloride and a dialkyl ether wherein the mole ratio of dialkyl ether to titanium tetrachloride is at least 0.1 and the concentration of titanium tetrachloride is maintained at at least 1 volume percent of the liquid phase, said dialkyl ether having the formula R'OR", in which R' and R" are the same or different and each are selected from the group consisting of (a) alkyl groups having 1 to 4 carbon atoms, (b) normal alkyl groups having 5 carbon atoms, and (c) alkyl groups having 6-20 carbon atoms.
Claim 3
Dependent Claim
14 words
A process according to claim 1, wherein the organoaluminum compound is diethyl aluminum chloride.
Claim 4
Dependent Claim
14 words
A process according to claim 1, wherein the organoaluminum compound is ethyl aluminum dichloride.
Claim 5
Dependent Claim
37 words
A process according to claim 1, wherein the reduction of titanium tetrachloride is effected at a temperature of -50° to +30° C. and thereafter the temperature of the reaction mixture is raised to 20° to 120° C.
Claim 6
Dependent Claim
30 words
A process according to claim 1, wherein the aluminum compounds are removed by complexing with an ether and then extracting the ehter complex of the aluminum compounds with a solvent.
Claim 7
Dependent Claim
44 words
A process according to claim 5, wherein the ether complexing agent is selected from the group consisting of diethyl ether, diisopropyl ether, di-n-butyl ether, di-isobutyl ether, diisoamyl ether, di-2-ethylhexyl ether, di-2-ethylheptyl ether, allyl ethyl ether, allyl butyl ether, anisole, phenetole, chloroanisole, bromoanisole and dimethoxybenzene.
Claim 8
Dependent Claim
58 words
A process according to claim 1, wherein the alkyl ether employed in mixture or complexed with titanium tetrachloride is an alkyl ether selected from the group consisting of di-n-propyl ether, diisopropyl ether, di-n-butyl ether, diisobutyl ether, isobutyl-n-butyl ether, di-n-amyl ether, di-n-hexyl ether, di-n-heptyl ether, diisoheptyl ether, di-2-ethylhexyl ether, di-n-dodecyl ether, n-butyl-2-ethylhexyl ether, and isobutyl-2-ethylhexyl ether and mixtures thereof.
Claim 9
Dependent Claim
13 words
A process according to claim 7, wherein the alkyl ether is di-n-amyl ether.
Claim 10
Dependent Claim
24 words
A process according to claim 2, wherein the mol ratio of the diethyl aluminum chloride to titanium tetrachloride is 1 or more to 1.
Claim 11
Dependent Claim
25 words
A process according to claim 3, wherein the mol ratio of ethyl aluminum dichloride to titanium tetrachloride is 0.3 to 1 to 1.2 to 1.
Claim 12
Dependent Claim
10 words
The catalyst component produced by the process of claim 1.
Claim 13
Dependent Claim
10 words
The catalyst component produced by the process of claim 9.
Claim 14
Dependent Claim
10 words
The catalyst component produced by the process of claim 10.
Claim 15
Dependent Claim
10 words
The catalyst component produced by the process of claim 4.
Claim 16
Dependent Claim
10 words
The catalyst component produced by the process of claim 5.
Claim 17
Dependent Claim
10 words
The catalyst component produced by the process of claim 6.
Claim 18
Dependent Claim
10 words
The catalyst component produced by the process of claim 7.
Claim 19
Dependent Claim
10 words
The catalyst component produced by the process of claim 8.
Claim 20
Dependent Claim
72 words
A process according to claim 1, wherein, in said contacting of brown or black-brown titanium trichloride reduced solid in an inert diluent with said activator, the mole ratio of the dialkyl ether to titanium trichloride is within the range of 0.1 to 2.0, the concentration of titanium tetrachloride in the diluent is at least 5 volume percent and the reduced solid concentration in the diluent is at least 50 grams per liter.