Hydrocarbon polymer modifiers with high aromaticity and uses thereof
A technology of hydrocarbon polymer and modifier, applied in the field of hydrocarbon polymer resin, which can solve the problems of reduced cohesive strength and high temperature resistance of adhesives
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[0121] Preparation of rubber compositions
[0122] The rubber composition is manufactured in a suitable mixer using two successive stages of preparation: a first stage ( sometimes referred to as the "non-production" stage), followed by a second stage (sometimes referred to as the "production" stage) of machining at lower temperatures (usually below 110°C, such as 60°C to 100°C), finishing here A crosslinking or vulcanization system is introduced during stages; these stages have been described, for example, in applications EP-A-0 501 227, EP-A-0 735 088, EP-A-0 810 258, WO 00 / 05300 or WO 00 / 05301 described.
[0123] The first (non-production) stage is carried out in several thermomechanical stages. During the first step, the elastomers, reinforcing fillers and hydrocarbon polymer modifiers (and optionally, coupling agents and / or other The ingredients, with the exception of the crosslinking system, are introduced into a suitable mixer (eg a conventional internal mixer). Afte...
Embodiment 1
[0160] Analysis of Prior Art Hydrocarbon Polymer Additives
[0161] Tg and %HAr of prior art resins with at least one elastomer and prior art hydrocarbon polymer additives were evaluated. The first set of prior art additive samples (PA1, PA2, PA3, PA4, and PA5) each had: (a) from about 40% to about 80% by weight of dicyclopentadiene, cyclopentadiene, based on the total weight of the polymer additive and methylcyclopentadiene derived content: (b) a weight average molecular weight of about 100 g / mole to about 800 g / mole; and (c) a softening point determined according to ASTM D6090 of about 110°C to about 150°C. These dicyclopentadiene resins also include aromatic compounds such as styrene, xylene, alpha-methylstyrene, vinyltoluene and indene, as well as non-aromatic compounds such as linear C4 to C6 fractions or isomers thereof. Dicyclopentadiene-based additive and elastomer combinations have been shown to improve performance characteristics in tires, such as high wet traction ...
Embodiment 2
[0180] Analysis of HPM of the Invention
[0181] HPM samples 5 to 9 were prepared by varying the feed stream in a thermal polymerization unit known to achieve a certain cloud point of the tackifier. After processing in the thermal polymerization unit, the tackifier was nitrogen stripped at 200°C. The properties of the hydrocarbon polymer modifiers are provided in Tables 5A, 5B, 6A and 6B below. The modifiers described herein can be prepared by known methods. See, eg, Kirk-Othmer Encyclopedia of Chemical Technology, 4th Edition, Vol. 13, pp. 717-744. One method is to thermally polymerize petroleum fractions. Polymerization can be batch, semi-batch or continuous. Thermal polymerization is generally carried out at a temperature of 160°C to 320°C, for example at about 260°C to 280°C, for a period of 0.5 to 9 hours, usually 1.0 to 4 hours. Thermal polymerization is usually carried out in the presence or absence of an inert solvent.
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