Methods for improving production in gas phase polymerization
US-12152095-B2 · Nov 26, 2024 · US
US2025059307A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2025059307-A1 |
| Application number | US-202318726279-A |
| Country | US |
| Kind code | A1 |
| Filing date | Mar 7, 2023 |
| Priority date | Mar 10, 2022 |
| Publication date | Feb 20, 2025 |
| Grant date | — |
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Provided is an ethylene/1-hexene copolymer satisfying the following conditions, having excellent long-term stability and processability as well as pipe resistance to internal pressure, and being useful for manufacturing high-pressure heating pipes, PE-RT pipes or large-diameter pipes,a molecular weight distribution (Mw/Mn) is 8 to 12,a broad orthogonal co-monomer distribution (BOCD) is 1 to 2,an integral value in the region where Log M is 6 or more in a gel permeation chromatography GPC curve graph having an x-axis of log M and a y-axis of dw/dlogM is 3.0% or more of the total integral value, anda tie molecule fraction is 6.0% or more.
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1 . An ethylene/1-hexene copolymer satisfying the following conditions: a molecular weight distribution (Mw/Mn) is 8 to 12, (a broad orthogonal co-monomer distribution) (BOCD) is 1 to 2, an integral value in a region where Log M is 6 or more in a gel permeation chromatography (GPC) curve graph having an x-axis of log M and a y-axis of dw/dlogM is 3.0% or more of a total integral value, wherein the log M is a a log value of a weight average molecular weight, and the dwt/dlog M is a molecular weight distribution, and a tie molecule fraction is 6.0% or more. 2 . The ethylene/1-hexene copolymer of claim 1 , wherein the molecular weight distribution (Mw/Mn) is 10 to 11.8. 3 . The ethylene/1-hexene copolymer of claim 1 , wherein the BOCD is 1.04 to 1.8. 4 . The ethylene/1-hexene copolymer of claim 1 , wherein the integral value in the region where Log M is 6 or more in a GPC curve graph having an x-axis of log M and a y-axis of dw/dlogM is 3.03% or more of the total integral value. 5 . The ethylene/1-hexene copolymer of claim 1 , wherein the tie molecule fraction is 6.05% or more. 6 . The ethylene/1-hexene copolymer of claim 1 , which has a density measured according to ASTM D 1505 is of 0.945 g/cm 3 to 0.955 g/cm 3 . 7 . The ethylene/1-hexene copolymer of claim 1 , which has a melt index (MI 2.16 ) measured at 190° C. under a load of 2.16 kg according to ASTM D 1238 0.05 g/10 min to 0.25 g/10 min. 8 . The ethylene/1-hexene copolymer of claim 1 , which has a high-load melt index (HLMI, MI 21.6 ) measured at 190° C. under a load of 21.6 kg according to ASTM D 1238 is of 10 g/10 min to 18 g/10 min. 9 . The ethylene/1-hexene copolymer of claim 1 , which has a melt flow rate ratio (MI 21.6 /MI 2.16 ) measured at 190° C. according to ASTM D 1238 is of 85 to 120. 10 . The ethylene/1-hexene copolymer of claim 1 , which has a characteristic stress measured according to ASTM D 638 is of 13 MPa to 14.5 MPa. 11 . The ethylene/1-hexene copolymer of claim 1 , which has a resistance to internal pressure measured according to ISO 9080 of 10 MPa to 12 MPa. 12 . The ethylene/1-hexene copolymer of claim 1 , which has a strain hardening modulus, which is a slope of a linear fitting value between a true strain 8 and 12 in a Hookean constitutive model curve after measuring a strain/stress curve under 80° C. and 20 mm/min in accordance with ISO 18488 to obtain a Neo-Hookean constitutive model curve having a x-axis of λ 2 −1/λ, and a y-axis of σ true of 23 MPa to 25 MPa. 13 . The ethylene/1-hexene copolymer of claim 1 , which has a notch pipe test (NPT) result according to ISO 13479 of 1500 to 4000 hours. 14 . The ethylene/1-hexene copolymer of claim 1 , wherein a 1-hexene content in the ethylene/1-hexene copolymer is 3.0 wt % to 7.0 wt % based on a total weight of the ethylene/1-hexene copolymer. 15 . A method for preparing the ethylene/1-hexene copolymer according to claim 1 , comprising copolymerizing ethylene and 1-hexene in a mono-modal polymerization process in the presence of a catalyst composition comprising a first metallocene compound represented by Chemical Formula 1 and a second metallocene compound represented by Chemical Formula 2 while introducing hydrogen gas, wherein the first metallocene compound and the second metallocene compound are included in a molar ratio of 1:2 to 1:8: (Cp 1 R a ) n (Cp 2 R b )M 1 Z 3-n 1 [Chemical Formula 1] in Chemical Formula 1, M 1 is a Group 4 transition metal; each of Cp 1 and Cp 2 is independently cyclopentadienyl unsubstituted or substituted with C 1-20 hydrocarbon; R a and R b are the same as or different from each other, and are each independently hydrogen, C 1-20 alkyl, C 1-20 alkoxy, C 2-20 alkoxyalkyl, C 6-20 aryl, C 6-20 aryloxy, C 2-20 alkenyl, C 7-40 alkylaryl, C 7-40 arylalkyl, C 8-40 arylalkenyl, C 2-20 alkynyl, or substituted or unsubstituted C 2-20 heteroaryl containing at least one N, O or S, provided that at least one of R a or R b is not hydrogen; Z 1 are each independently halogen, C 1-20 alkyl, C 2-20 alkenyl, C 7-40 alkylaryl, C 7-40 arylalkyl, C 6-20 aryl, substituted or unsubstituted C 1-20 alkylidene, substituted or unsubstituted amino, C 2-20 alkylalkoxy, or C 7-40 arylalkoxy; and n is 1 or 0, in Chemical Formula 2, M 2 is a Group 4 transition metal; A is carbon, silicon, or germanium; X 1 and X 2 are the same as or different from each other, and are each independently halogen, or C 1-20 alkyl; R 1 to R 4 are the same as or different from each other, and are each independently hydrogen, C 1-20 alkyl, C 2-20 alkenyl, C 6-20 aryl, C 7-20 alkylaryl, or C 7-20 arylalkyl, or two or more substituents adjacent to each other of R 1 to R 4 are connected with each other to form a substituted or unsubstituted aliphatic ring, a substituted or unsubstituted aromatic ring, or a substituted or unsubstituted heteroaromatic ring containing at least one N, O or S; R 5 and R 6 are the same as or different from each other, and are each independently C 1-20 alkyl, C 2-20 alkenyl, C 6-30 aryl, or C 2-20 alkoxyalkyl; and R 7 is C 1-20 alkyl, C 2-20 alkenyl, or C 6-30 aryl. 16 . The method of claim 15 , wherein the first metallocene compound is represented by any one of the following structural formulae: 17 . The method of claim 15 , wherein the second metallocene compound is represented by any one of the following structural formulae: 18 . The method of claim 15 , wherein the mono-modal polymerization process is performed in a single loop slurry reactor. 19 . The method of claim 15 , wherein the 1-hexene is included in an amount of 4.0 wt % to 6.0 wt % based on a total weight of the ethylene in the copolymerization process. 20 . A pipe comprising the ethylene/1-hexene copolymer of claim 1 .
as weight or mass percentages · CPC title
Melt flow index or melt flow ratio · CPC title
High density, i.e. > 0.95 g/cm3 · CPC title
Impact strength or impact resistance, e.g. Izod, Charpy or notched · CPC title
Cp or analog bridged to a non-Cp X anionic donor · CPC title
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