Preparation of multimodal, high density, ethylene homopolymer barrier resins and films
a technology of homopolyethylene and barrier resin, which is applied in the direction of synthetic resin layered products, layered products, chemistry apparatus and processes, etc., can solve the problems of complex coextusion process, high cost and complexity of producing multilayer films, and increase the cost and complexity of producing these films. , to achieve the effect of high density
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example 1
[0025]A Ziegler-Natta catalyst is prepared by reacting or mixing titanium tetrachloride, ethylaluminum dichloride, polymethylhydridosiloxane, dibutyl magnesium, ethylaluminium dichloride, and tetraisopropyltitanate in accordance with the general procedure disclosed in U.S. Pat. No. 4,511,669. The catalyst is slurried with hexane to the desired titanium concentration. Hexane, the catalyst slurry, triethylaluminum (TEAL) cocatalyst, cyclohexylmethyldimethoxy-silane (CMDS) modifier, ethylene, hydrogen and antistatic agent (oleylbis(2-hydroxyethyl)amine) are continuously fed to a first reactor in amounts given in Table 1 to produce a low molecular weight, homopolyethylene component. Melt index MI2 and density of the first homopolyethylene component are listed in Table 1.
[0026]The reaction mixture from the first reactor is continuously transferred to a flash drum where hydrogen and unreacted ethylene are removed. The reaction mixture recovered from the flash drum containing the homopolye...
example 3
[0029]Example 1 is essentially repeated but the catalyst is prepared by reacting or mixing titanium tetrachloride, ethylaluminum dichloride, polymethylhydridosiloxane, dibutyl magnesium, ethylaluminium dichloride, ethanol and isopropanol in accordance with the general procedure disclosed in U.S. Pat. No. 4,464,518 and diluted with hexane to the desired titanium concentration. Feed rates and polymerization conditions employed in the first and second reactors and properties of the first homopolyethylene component and final barrier resin product are reported in Table 1.
TABLE 1Ex. No.Ex.1C. Ex. 2Ex.3First Reactor PolymerizationPressure (psig)9071106Temperature (° C.)808080Ethylene (lbs / hr)29.229.229.4Antistatic agent (lbs / hr)0.00160.00180.007Hexane (lbs / hr)166166166Catalyst Slurry (moles0.001690.001250.00372Ti / hr)Cocatalyst (moles / hr)0.0660.0850.159CMDS (ppm based on16016hexane)H2 / Ethylene molar ratio1.92.12.7(vapor space)First Reactor Polymer PropertiesMI2 (g / 10 min)141446Density (g / cm...
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