Iron Oxide-Based Catalyst for Catalytic Cracking of Heavy Oil

E. Fumoto, Shinya Sato, T. Takanohashi
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引用次数: 2

Abstract

This chapter describes an iron oxide catalyst containing Zr and Al for production of light hydrocarbons by catalytic cracking of petroleum residual oil in a steam atmosphere. The catalyst was hematite structure and useful for decomposition and desulfurization of resid- ual oil. After lattice oxygen of iron oxide reacted with heavy oil fraction of residual oil, oxygen species generated from steam were supplied to iron oxide lattice and reacts with heavy oil fraction, producing light hydrocarbons and carbon dioxide. When the oxygen species were generated from steam, hydrogen species were simultaneously generated from steam. The hydrogen species were transferred to light hydrocarbons, hydrogen sulfide, and residue deposited on the catalyst. Supplies of the hydrogen species to light hydrocar- bons suppressed alkene generation. Generation of hydrogen sulfide indicated decomposi tion of sulfur compounds of residual oil. The sulfur concentration of product oil decreased compared to the concentration of residual oil. Some oxygen species could be transferred to sulfur dioxide. Accordingly, hydrogenation and oxidation by the hydrogen and oxygen species derived from steam provided the decomposition and desulfurization of residual oil with the iron oxide-based catalyst in a steam atmosphere.
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重油催化裂化用氧化铁基催化剂
本章描述了一种含Zr和Al的氧化铁催化剂,用于在蒸汽气氛下催化裂解石油渣油生产轻烃。催化剂为赤铁矿结构,可用于渣油的分解和脱硫。氧化铁晶格氧与剩余油重油馏分反应后,蒸汽生成的氧供给氧化铁晶格与重油馏分反应,生成轻烃和二氧化碳。当蒸汽生成氧时,蒸汽同时生成氢。氢转化为轻烃、硫化氢和残渣沉积在催化剂上。向轻烃烃类提供氢抑制了烯烃的生成。硫化氢的产生表明残油中硫化物的分解。成品油的硫浓度比渣油的硫浓度降低。一些氧可以转化为二氧化硫。因此,来自蒸汽的氢和氧的加氢和氧化提供了在蒸汽气氛中用氧化铁基催化剂分解和脱硫渣油。
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