Apparatus and method for removing voc from polypropylene and reducing odor level by steaming process
US-2024043579-A1 · Feb 8, 2024 · US
US11267910B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11267910-B2 |
| Application number | US-201816613655-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 9, 2018 |
| Priority date | May 18, 2017 |
| Publication date | Mar 8, 2022 |
| Grant date | Mar 8, 2022 |
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A catalyst mixture made from or containing (a) particles of a solid catalyst component comprising Ti, Mg, Cl, and (b) from 0.5 to 5.0% by weight, based upon the total weight of the mixture, of particles of a solid compound having particle size ranging from 0.1 μm to 1 mm containing more than 50% by weight of SiO2 units.
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What is claimed is: 1. A catalyst mixture comprising: a mechanical mixture of (a) particles of a solid catalyst component comprising titanium (Ti), magnesium (Mg), and chloride (Cl), and (b) from 0.2 to 5.0% by weight, based upon the total weight of the catalyst mixture (a)+(b), of particles of a solid compound having a particle size ranging from 0.1 μm to 1 mm and containing more than 50% by weight of SiO 2 units. 2. The catalyst mixture of claim 1 wherein the solid compound (b) containing more than 50% by weight of SiO 2 units is selected from the group consisting of silica, silicates, diatomaceous earth, and a combination thereof. 3. The catalyst mixture of claim 2 wherein the solid compound (b) containing more than 50% by weight of SiO 2 units is a silicate selected from phyllosilicates. 4. The catalyst mixture of claim 3 wherein the phyllosilicate is talc. 5. The catalyst mixture of claim 1 wherein the solid compound (b) has particle size ranging from 2 to 800 μm. 6. The catalyst mixture of claim 1 wherein the solid compound (b) containing more than 50% by weight of SiO 2 units is a silica. 7. The catalyst mixture of claim 6 wherein the silica is crystalline silica. 8. The catalyst mixture of claim 7 wherein the crystalline silica has a particle size ranging from 0.1 to 5 μm. 9. The catalyst mixture of claim 1 wherein the particle size of the solid catalyst component (a) ranges from 4 to 120 μm. 10. The catalyst mixture of claim 9 wherein the solid catalyst component (a) has a sphericity factor higher than 0.60. 11. The catalyst mixture of claim 10 wherein the solid catalyst component (a) has a sphericity factor higher than 0.7 and a particle size ranging from 10 to 90 μm. 12. The catalyst mixture according to claim 1 , wherein the amount of particles of solid compound (b) ranges from 0.5 to 5% wt, based on the total weight of catalyst mixture (a)+(b). 13. The catalyst mixture of claim 1 , wherein the solid catalyst component (a) further comprises an electron donor selected from the group consisting of esters, ethers, amines, silanes, carbamates and ketones and mixtures thereof. 14. A catalyst system for the homopolymerization or copolymerization of olefins CH 2 ═CHR, wherein R is hydrogen or a hydrocarbyl radical with 1-12 carbon atoms, comprising: the product obtained by contacting: (i) the catalyst mixture according to claim 1 ; (ii) an alkylaluminum compound and, (iii) optionally an external electron donor compound. 15. A process for the homopolymerization or copolymerization of olefins CH 2 ═CHR, wherein R is hydrogen or a hydrocarbyl radical with 1-12 carbon atoms, carried out in the presence of the catalyst system according to claim 14 .
Metal oxides · CPC title
Catalysts comprising at least two different metals, in metallic form or as compounds thereof, in addition to the component covered by group C08F4/64 {(C08F4/64003 - C08F4/64196 take precedence)} · CPC title
Carriers therefor · CPC title
Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond · CPC title
Mixing {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
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