Apparatus and method for removing voc from polypropylene and reducing odor level by steaming process
US-2024043579-A1 · Feb 8, 2024 · US
US10435490B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10435490-B2 |
| Application number | US-201615750391-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 14, 2016 |
| Priority date | Aug 4, 2015 |
| Publication date | Oct 8, 2019 |
| Grant date | Oct 8, 2019 |
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A Prepolymerized catalyst component for the polymerization of olefins comprising a solid catalyst component which comprises Mg, Ti, and chlorine atoms and an electron donor (ID) said prepolymerized catalyst component being characterized by the fact that: the electron donor (ID) is constituted by at least 80% mol of 1,3 diethers with respect to the total molar amount of electron donor compounds; the prepolymerized catalyst has a porosity due to pores with diameters up to 1 μm of less than 0.2 cm3/g; it contains an amount of ethylene prepolymer of less than 45% with respect to the total weight of prepolymerized catalyst.
Opening claim text (preview).
What is claimed is: 1. A prepolymerized catalyst component for the polymerization of olefins comprising a solid catalyst component which comprises Mg, Ti, and chlorine atoms and an electron donor (ID), said prepolymerized catalyst component being characterized by: the electron donor (ID) comprises at least 80% mol of 1,3-diethers with respect to the total molar amount of electron donor compounds; the prepolymerized catalyst has a porosity due to pores with diameters up to 1 μm of less than 0.2 cm 3 /g; and the said prepolymerized catalysts component comprises an amount of ethylene prepolymer of less than 45% with respect to the total weight of prepolymerized catalyst. 2. The prepolymerized catalyst component according to claim 1 , wherein the ID/Mg molar ratio ranges from 0.030 to 0.20. 3. The prepolymerized catalyst component according to claim 1 , wherein the ID/Mg molar ratio ranges from 0.035 to 0.15. 4. The prepolymerized catalyst component according to claim 1 , wherein the Mg/Ti molar ratio ranges from 4 to 10. 5. The prepolymerized catalyst component according to claim 1 , in which the amount of ethylene pre-polymer is less than 40% wt based on the total weight of pre-polymerized solid catalyst component. 6. The prepolymerized catalyst component according to claim 4 , in which the amount of ethylene pre-polymer ranges from 15 to 35% wt based on the total weight of pre-polymerized solid catalyst component. 7. The prepolymerized catalyst component according to claim 1 , having an average particle size ranging from 20 to 100 μm. 8. The prepolymerized catalyst component according to claim 1 , in which the porosity is less than 0.15 cm 3 /g. 9. The prepolymerized catalyst component according to claim 1 , in which the porosity ranges from 0.05 to 010 cm 3 /g. 10. The prepolymerized catalyst component according to claim 1 , in which the electron donor compound (ID) is selected from the compounds 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 one or more cyclic structures; the R III groups, equal or different from each other, are hydrogen or C 1 -C 18 hydrocarbon groups; the R IV groups equal or different from each other, have the same meaning of R III except that they cannot be hydrogen; and each of the R I to R IV groups optionally contains heteroatoms selected from halogens, N, O, S and Si. 11. The prepolymerized catalyst component according to claim 1 , wherein the electron donor (ID) is selected among 1,3-diethers of formula (III): where the R III and R IV radicals have the same meaning defined in formula (I), R VI radicals equal or different are hydrogen; halogens, selected from 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 one or more heteroatoms selected from the group consisting of N, O, S, P, Si, Cl and F, as substitutes for carbon or hydrogen atoms, or both. 12. The pre-polymerized catalyst according to claim 1 , comprising a Ti-halogen bond and a Mg halide. 13. A catalyst system for the polymerization of olefins CH 2 ═CHR, in which R is hydrogen or a hydrocarbyl radical with 1-12 carbon atoms, comprising the product of the reaction between: (i) the prepolymerized solid catalyst component according to claim 1 , (ii) an alkylaluminum compound and optionally (iii) an external electron donor compound. 14. A catalyst system according to claim 13 , in which the external electron donor is selected from silicon compounds of formula Ra 5 Rb 6 Si(OR 7 )c, where a and b are integer from 0 to 2, c is an integer from 1 to 3 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 selected from N, O, halogen and P. 15. A gas-phase process for the polymerization of olefins CH 2 ═CHR, wherein R is hydrogen or a C 1 -C 12 hydrocarbyl group, comprising contacting the olefins with the catalyst system according to claim 13 .
Ethene · CPC title
Propene · CPC title
halides of magnesium · CPC title
containing aliphatic unsaturation · CPC title
containing silicium · CPC title
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