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CATALYTIC CRACKING METHOD AND CATALYTIC CRACKER USED THEREIN

机译:催化裂化方法及其所用的催化裂化器

摘要

PROBLEM TO BE SOLVED: To provide a catalytic cracking method wherein a hydrolysis reaction and a decarboxylation reaction are carried out separately in catalytic cracking of a raw material biomass to promote the hydrolysis reaction for sufficiently decomposing the raw material biomass into fatty acid; a decomposition product principally consisting of the fatty acid obtained by the hydrolysis is subjected to catalytic cracking with a decarboxylation cracking catalyst to promote progress of the decarboxylation reaction for improving a recovery ratio of a kerosene and light oil fraction in a cracked oil; and high quality cracked oil can be obtained with a short reaction time since the hydrolysis reaction and the decarboxylation reaction are advanced quickly.;SOLUTION: A catalytic cracking method has a constitution including a hydrolysis step of bringing a hydrolysis catalyst and raw material biomass into mutual contact in a first reaction vessel heated to 350-475°C to hydrolyze the raw material biomass and obtaining a decomposition product principally consisting of fatty acid; and a decarboxylation step of bringing a decarboxylation cracking catalyst and the fatty acid into mutual contact in a second reaction vessel heated to 350-475°C to decarboxylate the fatty acid.;COPYRIGHT: (C)2014,JPO&INPIT
机译:解决的问题:提供一种催化裂化方法,其中在原料生物质的催化裂化中分别进行水解反应和脱羧反应,以促进水解反应以将原料生物质充分分解为脂肪酸。将主要由水解得到的脂肪酸组成的分解产物用脱羧裂化催化剂进行催化裂化,以促进脱羧反应的进行,从而提高裂化油中煤油和轻油馏分的回收率。由于水解反应和脱羧反应的进行较快,因此可以在较短的反应时间内获得高质量的裂化油。;解决方案:催化裂化法的结构包括将水解催化剂和原料生物质相互转化的水解步骤。在加热至350-475℃的第一反应容器中接触以水解原料生物质并获得主要由脂肪酸组成的分解产物;脱羧步骤:使脱羧裂化催化剂与脂肪酸在加热至350-475℃的第二反应容器中相互接触以使脂肪酸脱羧。; COPYRIGHT:(C)2014,JPO&INPIT

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