1526295 Reducing CO-emission in the regeneration of fluidised cracking catalysts TEXACO DEVELOPMENT CORP 5 Dec 1975 [23 Dec 1974] 49955/75 Heading B1E In the regeneration of a coked fluidized cracking catalyst the catalyst is fed into a dense fluidized catalyst phase in a regenerator maintained at 1275-1355‹F with a residence time of 3-10 min., fluidizing the dense phase and burning off the coke with a flow of regeneration gas sufficient to maintain a 1-10mol% O 2 excess in the flue gas and simultaneously adjusting said temperature and O 2 excess to control the afterburn so that the dilute phase which is in direct communication with the dense phase is maintained at 1375-1455‹F without extraneous cooling.
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机译:1526295减少流化裂化催化剂再生中的CO排放TEXACO DEVELOPMENT CORP 1975年12月5日[1974年12月23日] 49955/75标题B1E在再生焦化流化裂化催化剂中,将催化剂送入再生器中的致密流化催化剂相中保持在1275-1355 ‹F,停留时间为3-10分钟,流化致密相,并使用足以保持烟道气中过量1-10mol%O 2的再生气体流将焦炭燃烧掉调节所述温度和过量的O 2以控制加力燃烧,使与致密相直接连通的稀相保持在1375-1455°F,而无需额外的冷却。
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