Development and application of a fluid catalytic cracking gasoline hydro-upgrading process GARDES
3rd World Congress on Petrochemistry and Chemical Engineering
November 30-December 02, 2015 Atlanta, USA

Xiaojun Bao1 and Yu Fan2

1Fuzhou University, China 2China University of Petroleum, China

Scientific Tracks Abstracts: J Pet Environ Biotechnol

Abstract:

More than 90% of sulfur-containing compounds and about 90% of olefins in typical refinery gasoline pools come from Fluid Catalytic Cracking (FCC) gasoline, thus the sulfur and olefin reduction of this stream is crucial for producing clean gasoline. It has been widely recognized that hydrotreating is the most important technique for producing clean transportation fuels in industrial practice, but the existing techniques can hardly accomplish the objectives of both deep Hydrodesulfurization (HDS) and olefin reduction of FCC gasoline with acceptable loss in gasoline Research Octane Number (RON). To solve this problem, we developed a novel process, GARDES, by coupling high-efficient HDS and directed olefin conversion. First, the full-range FCC gasoline is prehydrogenated and then split into light and heavy cracked naphthas (LCN and HCN) through distillation, in which the LCN has a very low sulfur content and thus can be directly used for product blending and the HCN contains a relatively lower concentration of olefins but most ulfur-containing compounds; second, the HCN with high sulfur content is hydrotreated over a selective HDS catalyst with high desulfurization activity but low olefin saturation activity; third, the hydrodesulfurized HCN is further treated over an octane recovery catalyst to convert olefins into isoparaffins and aromatics with high RONs; finally, a clean gasoline blending component that meets both Euro IV and Euro V standards is obtained by mixing the resultant HCN and LCN. The GARDES process is featured by having ultradeep HDS, significant olefin reduction, and excelllent RON preservation abilities. Up to date, we have issued over 20 licenses to refineries and successfully erected 15 industrial units with a total annual processing capacity of more than 15 million tons.

Biography :

Xiaojun Bao obtained his PhD in 1990 in the Chinese Academy of Sciences. He is now Professor and the Dean of the College of Chemical Engineering, Fuzhou University. He has published more than 200 papers in reputed journals, owns more than 70 granted patents, and has been serving as an Editorial Board Member of several journals such as Fuel Processing Technology, Chinese Journal of Chemical Engineering, Petroleum Science, and Journal of Coal Chemistry and Engineering.

Email: baoxj@fzu.edu.cn