Methods for improving production in gas phase polymerization
US-12152095-B2 · Nov 26, 2024 · US
US10626202B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10626202-B2 |
| Application number | US-44908208-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 15, 2008 |
| Priority date | Feb 1, 2007 |
| Publication date | Apr 21, 2020 |
| Grant date | Apr 21, 2020 |
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Monomodal copolymers of ethylene and molding compositions comprising such copolymers, wherein the copolymers have a density determined according to DIN EN ISO 1183-1, variant A in the range from 0.938 to 0.944 g/cm3, a melt index MFR21 determined according to ISO 1133 at 190° C. under a load of 21.6 kg in the range from 12 to 17 g/10 min, a weight average molar mass Mw in the range from 140 000 g/mol to 330 000 g/mol, a polydispersity Mw/Mn in the range from 9 to 17, and a content of comonomer side chains per 1000 carbon atoms Cx equal to or above a value defined via equation (I) Cx=128.7−134.62×d′, wherein d′ is the numerical value of the density of the copolymer in g/cm3, the use of the copolymers for producing injection-molded articles, as well as injection-molded articles comprising the copolymers, and process for the preparation of such monomodal copolymers.
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What is claimed is: 1. A process comprising: copolymerizing ethylene with at least one C 3 -C 12 1 -olefin to produce a monomodal copolymer comprising ethylene and at least one 1-olefin, wherein the monomodal copolymer has: (i) a M w in a range of from 150,000-300,000, (ii) a polydispersity M w /M n in a range of from 11-16, (iii) a density determined according to DIN EN ISO 1183-1, variant A of 0.940-0.942 g/cm 3 , (iv) a melt index MI 5 of 0.5-1 g/10 min, (v) a melt index MFR 21 (ISO 1133; 190° C., 21.6 kg) of 12-17 g/10 min, (vi) an environmental stress cracking resistance of 25-49 hours, and (vii) 0.1 to 10 C x comonomer side chains per 1000 carbon atoms, wherein C x is equal to or above a value defined by the equation (I) C x =128.7−134.62× d′ (I), wherein d′ is the numerical value of the density of the copolymer in g/cm 3 , (viii) 0.1-1% by weight of an additive; and (ix) a spiral length of greater than 40 cm at an MFR 21 of 14-15.6, and preparing an injection molded article comprising the monomodal copolymer of ethylene and at least one 1-olefin. 2. The process according to claim 1 , wherein ethylene and at least one C3-C12 1-olefin are copolymerized in the presence of a chromium catalyst. 3. The process according to claim 1 , wherein the copolymerization is conducted in at least one gas-phase reactor. 4. The process according to claim 1 , wherein the copolymerization is carried out at a temperature which is in a range restricted by an upper limit defined by equation (III) T H =173+6 d ′/(0.840− d ′) (III) and a lower limit defined by equation (IV) T L =178+7.3 d ′/(0.837− d ′) (IV) in which the variables have the following meanings: T H is the highest reaction temperature in ° C.; T L is the lowest reaction temperature in ° C.; and d′ is the numerical value of the density d of the copolymer to be synthesized. 5. The process according to claim 1 , wherein the injection molded article is selected from the group consisting of a cap, closure, screw cap, screw closure, tube shoulder, engineering part pipe fitting and fuel tank module part.
Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title
Melt flow index or melt flow ratio · CPC title
Polymerisation in gaseous state · CPC title
Melt tension or melt strength · CPC title
Oxides · CPC title
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