Apparatus and method for removing voc from polypropylene and reducing odor level by steaming process
US-2024043579-A1 · Feb 8, 2024 · US
US9453088B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9453088-B2 |
| Application number | US-73527808-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 22, 2008 |
| Priority date | Dec 28, 2007 |
| Publication date | Sep 27, 2016 |
| Grant date | Sep 27, 2016 |
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Prepolymerized catalyst component for the polymerization of olefins CH 2 ═CHR in which R is hydrogen or a hydrocarbyl radical with 1-12 carbon atoms, having average particle size equal to or lower than 30 μm comprising a solid catalyst component comprising magnesium halide, a titanium compound having at least a Ti-halogen bond and at least two electron donor compounds one of which being selected from 1,3-diethers and the other one being selected from esters of aromatic mono or dicarboxylic acids, said solid catalyst component being prepolymerized with an olefin, having from 2 to 10 carbon atoms, to such an extent that the amount of the olefin prepolymer is equal to or lower than 50 g per g of solid catalyst component.
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The invention claimed is: 1. Prepolymerized catalyst component for the polymerization of olefins CH 2 ═CHR wherein R is hydrogen or a hydrocarbyl radical with 1-12 carbon atoms, having an average particle size equal to, or lower than, 30 μm comprising a solid catalyst component which comprises magnesium halide, a titanium compound having at least a Ti-halogen bond and at least two electron donor compounds one of which being selected from 1,3-diethers and the other one being selected from esters of aromatic mono or dicarboxylic acids, said solid catalyst component being prepolymerized with an olefin, having from 2 to 10 carbon atoms, wherein the amount of the olefin polymer so obtained is equal to, or lower than, 50 g per g of solid catalyst component. 2. The prepolymerized catalyst component according to claim 1 wherein the 1,3-diethers are selected from those of formula (I): where R I and R II are the same or different and are hydrogen or linear or branched C 1 -C 18 hydrocarbon groups which can also form at least one cyclic structure; R III groups, equal or different from each other, are hydrogen or C 1 -C 18 hydrocarbon groups; and R IV groups equal or different from each other, have the same meaning of R III except that they cannot be hydrogen; and wherein each of the R I to R IV groups can contain heteroatoms selected from halogens, N, O, S and Si. 3. The prepolymerized catalyst component according to claim 2 wherein the 1,3-diethers are selected from the compounds of formula (III): where the R VI radicals equal or different are hydrogen; halogens, C 1 -C 20 alkyl radicals, linear or branched; C 3 -C 20 cycloalkyl, C 6 -C 20 aryl, C 7 -C 20 alkylaryl and C 7 -C 20 aralkyl radicals, optionally containing at least one heteroatom selected from the group consisting of N, O, S, P, Si and halogens, as substitutes for carbon or hydrogen atoms, or both; the radicals R III equal or different to each other, are selected from the group consisting of hydrogen; halogens; C 1 -C 20 alkyl radicals, linear or branched; C 3 -C 20 cycloalkyl, C 6 -C 20 aryl, C 7 -C 20 alkaryl and C 7 -C 20 aralkyl radicals; and R IV groups equal or different from each other, have the same meaning of R III except that they cannot be hydrogen; and wherein each of the R I to R IV groups can contain heteroatoms selected from halogens, N, O, S and Si. 4. The prepolymerized catalyst component according to claim 1 wherein the esters of aromatic mono or dicarboxylic acids compound are selected from phthalates. 5. The prepolymerized catalyst component according to claim 4 wherein said esters are C 1 -C 6 linear or branched alkyl esters of phthalic acids. 6. The prepolymerized catalyst component according to claim 1 wherein a molar ratio between the 1,3-diether and the ester donor is in the range of from 0.02 to 50. 7. A catalyst for the polymerization of olefins CH 2 ═CHR, wherein R is hydrogen or a hydrocarbyl radical with 1-12 carbon atoms, comprising the product of the reaction between: (i) a prepolymerized solid catalyst component having an average particle size equal to, or lower than, 30 μm comprising a solid catalyst component which comprises magnesium halide, a titanium compound having at least a Ti-halogen bond and at least two electron donor compounds one of which being selected from 1,3-diethers and the other one being selected from esters of aromatic mono or dicarboxylic acids, said solid catalyst component being prepolymerized with an olefin, having from 2 to 10 carbon atoms, wherein the amount of the olefin polymer so obtained is equal to, or lower than, 50 g per g of solid catalyst component; and (ii) an alkylaluminum compound. 8. The catalyst according to claim 7 further comprising an external electron donor compound. 9. The catalyst according to claim 8 wherein the electron donor compound is selected from silicon compounds of formula R a 5 R b 6 Si(OR 7 ) c , where a and b are integer from 0 to 2, c is an integer from 1 to 4 and the sum (a+b+c) is 4; R 5 , R 6 and R 7 are alkyl, cycloalkyl or aryl radicals with 1-18 carbon atoms, optionally containing heteroatoms. 10. The catalyst according to claim 9 wherein a is 1, b is 1 and c is 2. 11. A gas phase process for the (co)polymerization of olefins CH 2 ═CHR, wherein R is hydrogen or a hydrocarbyl radical with 1-12 carbon atoms, carried out in the presence of a catalyst comprising the product of the reaction between: (i) a prepolymerized solid catalyst component having an average particle size equal to, or lower than, 30 μm comprising a solid catalyst component which comprises magnesium halide, a titanium compound having at least a Ti-halogen bond and at least two electron donor compounds one of which being selected from 1,3-diethers and the other one being selected from esters of aromatic mono or dicarboxylic acids, said solid catalyst component being prepolymerized with an olefin, having from 2 to 10 carbon atoms, wherein the amount of the olefin polymer so obtained is equal to, or lower than, 50 g per g of solid catalyst component; (ii) an alkylaluminum compound; and (iii) optionally an external donor compound. 12. The prepolymerized catalyst component of claim 3 where the R VI radicals equal or different are Cl or F. 13. The prepolymerized catalyst component of claim 3 where the at least one heteroatom is Cl or F, as substitutes for carbon or hydrogen.
Pretreating with non-metals or metal-free compounds · CPC title
of titanium, zirconium or hafnium · CPC title
containing elements other than those covered by B01J31/0201 - B01J31/0255 · CPC title
Propene · CPC title
with alkaline earth metals, magnesium, beryllium, zinc, cadmium or mercury · CPC title
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