摘要
对K-Fe-MnO/Silicalite-2催化剂积炭及烧炭的差热与热重分析结果表明,在CO加氢反应过程中催化剂表面可形成两种类型的积炭,其中Ⅰ型炭有利于提高CO加氢制低碳烯烃的选择性,而Ⅱ型炭则不能。研究结果还表明,K-Fe-MnO/Silicalite-2催化剂经再生后可恢复其新鲜态催化剂性能。在单管扩大试验中,反应器入口高温区催化剂表面容易形成Ⅰ型和Ⅱ型积炭,而恒温区催化剂表面只有Ⅰ型积炭。
he differential thermal and thermo gravimetric analyses of K Fe MnO/silicalite 2 catalyst carbon deposit and carbon burning show that two types of carbon deposit may be formed on the catalyst surface during CO hydrogenation reaction, in which type I carbon deposit is advantagous to increase light olefins selectivity in CO hydrogenation, but type Ⅱ carbon deposit is not. The analytic results also show that K Fe MnO/silicalite 2 catalyst can be restored to its fresh state catalytic properties after regeneration. In the single tube scaleup tests, type Ⅰ and Ⅱ carbon deposits can easily be formed on the catalyst surface at the high temperature zone of the reactor inlet, and only type I carbon deposit is formed on the catalyst surface at the constant temperature zone, which will cause the displacement of the highest temperature zone in catalyst bed.
出处
《天然气化工—C1化学与化工》
CAS
CSCD
北大核心
1996年第6期33-36,共4页
Natural Gas Chemical Industry
基金
国家"八.五"重点科技攻关课题
关键词
合成气
烯烃
加氢
催化剂
一氧化碳
syngas
light olefins
CO hydrogenation
differential thermal and thermo gravimetric analyses