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C-01 lead the Department of arsenic removal catalyst in the import of mixed carbon carbon second three choices before the hydrogenation (selective hydrogenation of acetylene to ethylene, selective hydrogenation of acetylene C-propylene) arsenic removal catalyst on the basis of a modified, with a catalyst Long service life, removal of high activity, no hydrogenation reaction and so on. C-01 lead into the Department of arsenic removal catalyst reactor is subject to activation of activity after the main catalyst for removal of a small amount of water, the activation conditions are as follows: When activated, air or nitrogen heated to 100 ~ 230 ¡æ, with 100 to 800 of the Airspeed through the C-01 arsenic removal catalyst bed until the C-01 arsenic removal catalyst bed temperature rose to 100 ~ 200 ¡æ, to maintain the activation temperature of 24 to 48 hours (low-temperature, long time; small space, time Long), and then stop air, nitrogen-down to room temperature, the closure of stand-by. Dehydration can also be used for dealing with liquid nitrogen. Arsenic removal by the activated catalyst, is no longer required after the use of activated until deactivation. Parking off the replacement of arsenic before the first 100 ~ 150 ¡æ nitrogen replacement of 5 to 6 hours, nitrogen-cooled to room temperature. C-01 lead from the Department of arsenic has been a catalyst in the domestic petrochemical enterprises such as Shanghai Petrochemical, Beijing Yanshan Petrochemical, Jilin Petrochemical, and other units of mixed-ton carbon choose three lines before the hydrogenation (C selective hydrogenation of acetylene propylene) arsenic removal equipment unit On the use of carbon can be mixed in three 600 ~ 800ppb arsenic removal following 2ppb to improve the follow-up of carbon three selective hydrogenation catalyst life. In 2004 in Guangzhou Petrochemical Polypropylene plant for the removal of carbon monoxide in ethylene, ethylene can be in the removal of carbon monoxide to below 0.1ppm. |
3Â¥2008-10-12 10:44:40
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4Â¥2008-10-12 11:04:03
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5Â¥2008-10-12 11:05:58
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