Adhesive composition comprising amorphous propylene-ethylene copolymer and propylene polymer
a technology of amorphous propylene and propylene, which is applied in the direction of non-macromolecular adhesive additives, adhesives, adhesive additives, etc., can solve the problems of limited reactivity, poor bonding strength of amorphous olefins, and high cost of alpha-olefins
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example 1
[0158]In this example, various propylene-ethylene copolymers were produced in a two-liter stirred reactor with an average residence time of about one hour. The reactor temperature was maintained at approximately 140° C. and a pressure of 900 psig. The propylene was fed into the reactor as a liquid, while the ethylene was fed into the reactor as a gas. The polymerization occurred in the presence of a Ziegler-Natta catalyst, which was a titanium chloride on a magnesium chloride support. This particular catalyst is a heterogeneous-supported catalyst system formed from titanium compounds in combination with alkyl aluminum co-catalyst (“TEAL”). The catalyst system contained an Al / Ti mole ratio of 21. Any unreacted monomer and other vapors were vented from the reactor upon discharge of the copolymer.
[0159]Samples 1-11 were produced using the aforementioned catalyst system and an external electron donor. As noted below, the electron donor was either cyclohexylmethyldimethoxysilane (“C”) or...
example 2
[0165]In this example, various propylene-ethylene copolymers were produced using the process and system described in Example 1; however, the external electron donor used in this example was cyclohexylmethyldimethoxysilane. Furthermore, the amounts of electron donor added for each sample were varied as indicated by the donor / Ti molar ratio. The copolymers produced during this process are described in TABLE 2 below, along with their various properties and the reaction conditions used to produce them.
TABLE 2Copolymer Sample2A2B2C2D2E2F2GAl / Ti mole21212121212121ratioDonor / Ti,1.11.20.51.01.01.52.0mole ratioTEAL / Donor,31.329.670.032.932.924.716.5mole ratioHydrogen40202025252525(psig)Reactor140140140140140140140Temp, ° C.Reactor900900900900900900900Press.(psig)Catalyst843.91003.31006.81001.3957.2962.9904.1Activity(g / g)Visc. @3600660051754865726355384715190° C., cPSoftening140.3138.4145.3126.6135.9133129.6Point(° C.)Needle Pen.10141732242332(dmm)Wt. %10.010.010.015.013.015.015.0EthyleneFlow...
example 3
[0167]In this example, various propylene-ethylene copolymers were produced using the process and system described in Example 1. The external electron donor used in this example was dicyclopentyldimethoxysilane. Furthermore, the amounts of electron donor added for each sample was varied as indicated by the donor / Ti molar ratio. The copolymers produced during this process are described in TABLE 3 below, along with their various properties and the reaction conditions used to produce them
TABLE 3Copolymer SampleC1C23A3B3C3D3E3FAl / Ti mole2121212121212121ratioDonor / Ti,0.31.53.03.04.02.02.03.0mole ratioTEAL / Donor,71.015.87.07.05.210.410.47.0mole ratioHydrogen2025805050802550(psig)Reactor140140140140140140140140Temp, ° C.Reactor900900900900900900900900Press,(psig)Catalyst862.01037.1723.2793.4612.8880.6808.8630.1Activity(g / g)Visc. @761346251055315059631053164256250190° C., cPSoftening140.2143.2114.1109.997.4128.2136.4119.9Point(° C.)Needle Pen.2227374063212321(dmm)Wt. %10.015.015.017.517.513....
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