Alpha-olefin-styrene super molecular weight drag-reduction polymers and process for preparing the same
A technology of ultra-high molecular weight and styrene, applied in mechanical equipment, gas/liquid distribution and storage, pipeline systems, etc., can solve the problems of cumbersome operation process, high reaction heat, and high cost, and achieve cost reduction and reaction control temperature improvement , The effect of improving drag reduction efficiency
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Embodiment 1
[0010] Weigh 500kg of α-olefin with C number of 10, 460kg of α-olefin with C number of 12, 40kg of styrene, and mix well; 3 506g, organometallic catalyst Al(Et) 3 97g, mix well.
[0011] The tumbler of the cooling reaction device was cooled to -10°C and protected by nitrogen gas. Then the above two kinds of mixtures are uniformly dispersed on the surface of the drum through feeders of different sizes to form a thin film, and a bulk polymerization reaction takes place. In the reaction process, the linear velocity of the rotating drum is controlled to be 0.02m / min, and the polymerization reaction time is kept to be 1 hour.
[0012] The above-mentioned polymer is treated by α-olefin-styrene ultra-high molecular weight copolymer suspension dispersion process to form a dispersion system with a solid content of 40% of the above-mentioned polymer, which can be used as a drag reducer for long-distance pipelines of crude oil and refined oil.
[0013] In the special circuit for mea...
Embodiment 2
[0015] Weigh 600kg of α-olefin with C number of 8, 380kg of α-olefin with C number of 16, 20kg of styrene, and mix well; 3 438g, organometallic catalyst Al(Et) 2 Cl 121g, mix well.
[0016] The tumbler of the cooling reaction device was cooled to 0°C, and nitrogen protection was introduced. Then the above two kinds of mixtures are uniformly dispersed on the surface of the drum through feeders of different sizes to form a thin film, and a bulk polymerization reaction takes place. During the reaction process, the linear velocity of the drum was controlled to be 0.012 m / min, and the polymerization reaction time was kept to be 1 hour, and the polymer was scraped off by a scraper installed at the rear of the feeder.
[0017] The above-mentioned polymer is treated by α-olefin-styrene ultra-high molecular weight copolymer suspension dispersion process to form a dispersion system with a solid content of 45% of the above-mentioned polymer, which can be used as a drag reducer for lon...
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