Spherical magnesium halide adduct, a catalyst component and a catalyst for olefin polymerization prepared therefrom
US-9499569-B2 · Nov 22, 2016 · US
US10344103B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10344103-B2 |
| Application number | US-201515510665-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 11, 2015 |
| Priority date | Sep 11, 2014 |
| Publication date | Jul 9, 2019 |
| Grant date | Jul 9, 2019 |
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The Zigler-Natta catalyst composition of the present disclosure provides uniform polyethylene having a molecular weight in the range from 1 million g/mol to 12 million g/mol. The Zigler-Natta catalyst composition of the present disclosure comprises external electron donor selected from the group consisting of substituted silanediyl diacetate, trialkyl borate and tetraalkoxysilane.
Opening claim text (preview).
What is claimed is: 1. A Ziegler-Natta catalyst composition for preparation of an ultrahigh molecular weight polyolefin, said composition comprising: i. a pro-catalyst comprising a magnesium component and a titanium component; ii. an organo-aluminum co-catalyst; and iii. at least one external electron donor, wherein the at least one external electron donor is a substituted silanediyl diacetate or a trialkyl borate; wherein the magnesium component is in the form of a spheroidal magnesium alkoxide; and wherein the pro-catalyst is supported on silica and the mole ratio of the amount of silica to the amount of magnesium component ranges from 1:10 to 1:30, wherein the substituted silanediyl diacetate is selected from the group consisting of diethyl-2,2′-(dimethylsilanediyl)diacetate; diethyl-2,2′-(phenyl(methyl)silanediyl)diacetate and diethyl-2,2′-(diisopropylsilanediyl)diacetate, and wherein the trialkyl borate is selected from the group consisting of triethyl borate and trimethyl borate. 2. The catalyst composition as claimed in claim 1 , wherein the organo-aluminum co-catalyst is at least one selected from the group consisting of triethylaluminum, tridecylaluminum, tri-n-butylaluminum, tri-isopropylaluminum, tri-isoprenylaluminum, tri-isobutylaluminum, ethyl aluminum sesquichloride, diethylaluminum chloride, di-isobutyl aluminum chloride, triphenylaluminum, tri-n-octylaluminum and tri-n-decylaluminum. 3. The catalyst composition as claimed in claim 1 , wherein the mole ratio of the amount of the organo-aluminum co-catalyst to the amount of titanium component represented as elemental titanium ranges from 500:1 to 10:1. 4. The Ziegler-Natta catalyst composition as claimed in claim 1 , wherein the mole ratio of the amount of the organo-aluminum co-catalyst to the amount of the external electron donor ranges from 1:1 to 50:1. 5. A process for ethylene polymerization in the presence of the Ziegler-Natta catalyst composition as claimed in claim 1 ; said process comprising preparing a slurry of the Ziegler-Natta catalyst composition in a hydrocarbon solvent in a reactor and introducing ethylene in the reactor to attain a predetermined pressure followed by subjecting ethylene to polymerization at a temperature ranging from 50° C. to 100° C. for a time period ranging from 10 minutes to 120 minutes to obtain polyethylene. 6. The process as claimed in claim 5 , wherein the predetermined pressure of the ethylene ranges from 3 Kg/cm2 to 10 Kg/cm 2 . 7. The process as claimed in claim 5 , wherein the polymerization is carried out in the presence of a chain transfer agent. 8. The process as claimed in claim 7 , wherein said chain transfer agent is hydrogen.
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