ISSN 1008-5548

CN 37-1316/TU

Journal Online  2016 Vol.22
<Go BackNo.1

Experimental Research on Scaling Mechanism of Catalyst in Fluid Catalytic Cracking Flue Gas Turbine

WANG Yu1 , XING Shaowei1 , WANG Jianjun2

(1. Petrochemical General Plant, Sinopec Shengli Oil Field Co., Ltd., Dongying 257061, China; 2. College of Chemical Engineering, China University of Petroleum (East China), Qingdao 266580, China)

Abstract:Based on concentration, particle size and morphology analysis of catalyst samples from fluid catalytic cracking (FCC) unit of oil refinery, FCC flue gas turbine scale sample elemental composition analysis and high-temperature static sintering laboratory experiments,causes and influencing factors of catalyst scaling in gas turbine operating conditions were researched. The results show that the size of particles entered into the flue gas turbine is mainly less than 10 μm,and the shape of these particles is irregular which leads to easily deposited and adhered to the surface of flow passage component. Comparing with the FCC fresh catalyst, there are four kinds of metal elements which are Na, Ca, Fe, and Ni in the catalyst that entered into the flue gas turbine, and their contents significantly increase. The static sintering experiment in the high-temperature sintering furnace further validates the promoting effect of the four kinds of metal elements on catalyst scaling.

Keywords: scaling;catalyst; fluid catalytic cracking flue gas turbine

中图分类号:TQ051.1       文献标志码:A

文章编号:1008-5548(2016)01-0092-05

DOI:10.13732/j.issn.1008-5548.2016.01.022

收稿日期:2015-02-01, 修回日期:2015-02-25,在线出版时间:2016-02-22。

第一作者简介:王瑜(1963—),男,硕士,高级工程师,研究方向为石油加工工艺。 E-mail:wangyu993.slyt@sinopec.com。

通信作者简介:王建军(1971—),男,博士,副教授,研究方向为多相流分离。 电话:18653239578,E-mail:wangjianjun0992@126.com。