Bimodal ethylene-based polymers having high molecular weight high density fractions
A polymer, high-density technology, applied in the field of bimodal ethylene-based polymers, can solve the problems of property limitations, difficult to control component reactions, low bimodal polymers, etc.
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[0159] The following examples illustrate features of the disclosure, but are not intended to limit the scope of the disclosure.
example 1
[0161] A bimodal ethylene based polymer was formed using a loop reactor as the first reactor and a plug flow reactor as the second reactor. The feed stream to the first reactor contained 1206 pounds per hour (lb / hr) of ISOPAR-E solvent, 206 lb / hr of ethylene monomer, 82 lb / hr of hexene. Hydrogen was also introduced into the first reactor at 6200 seem. The ethylene concentration at the outlet of the first reactor was 30 g / L. The first catalyst introduced into the first reactor includes a main catalyst and a co-catalyst. The main catalyst is C with the following structure 67 h 88 o 4 Zr; Zirconium; Dimethyl[[2,2"'-[1,3-propanediylbis(oxygen- K O)]bis[3",5,5"-tris(1,1-dimethylethyl)-5'-methyl[1,1':3',1"-terphenyl]-2'- olato- K O]](2-)]:
[0162]
[0163] The main catalyst was added as needed to control the reactor outlet ethylene concentration of 30 g / L, and at the reactor outlet, the main catalyst loading was usually 0.09 μmol / L. The cocatalyst is bis(hydrogenated ta...
example 2
[0168] A bimodal ethylene based polymer was formed using a loop reactor as the first reactor and a plug flow reactor as the second reactor. The feed stream to the first reactor contained 1194 lb / hr of ISOPAR-E solvent, 206 lb / hr of ethylene monomer, 76 lb / hr of hexene. Hydrogen was also introduced into the first reactor at 7635 seem. The feed hexene / yield ratio was 8.0 and the feed hexene concentration was 6.9 wt%. The ethylene concentration at the outlet of the first reactor was 25 g / L. The first catalyst introduced into the first reactor includes a main catalyst and a co-catalyst. The main catalyst is C with the following structure 67 h 88 o 4 Zr; Zirconium; Dimethyl[[2,2"'-[1,3-propanediylbis(oxygen- K O)]bis[3",5,5"-tris(1,1-dimethylethyl)-5'-methyl[1,1':3',1"-terphenyl]-2'- olato- K O]](2-)]:
[0169]
[0170] Procatalyst was added as needed to maintain an ethylene concentration of 25 g / L. At the reactor outlet, the catalyst loading was about 0.12 μmol / L. Th...
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