Experimental Study on Homogeneous Catalytic Upgrading of Heavy Oil


如何引用文章

全文:

开放存取 开放存取
受限制的访问 ##reader.subscriptionAccessGranted##
受限制的访问 订阅存取

详细

Four catalyst precursors were prepared to assess the performance on the upgrading process of heavy oil. It has been showed that viscosity of Lukeqin heavy oil was decreased significantly, which revealed a viscosity reduction ratio of up to 99.28% with a catalyst precursor concentration of 0.12 wt %, reaction temperature of 365°С and reaction time of 40 min. Analysis of the oil after upgrading showed an obviously change in the composition of hydrocarbon components. The increase of light fractions after reaction improved the properties of heavy oil which is benefit to the pipeline transportation and downstream refining. Meanwhile, the mechanism of upgrading was also investigated. This work proved that heavy oil can be effectively upgraded with the catalyst precursor of petroleum acid iron.

作者简介

X. Tang

State Key Laboratory of Oil and Gas Reservoir Geology and Exploitation; College of Chemistry and Chemical Engineering

Email: Lijingjing771216@gmail.com
中国, Chengdu, 610500; Chengdu, 610500

X. Chen

State Key Laboratory of Oil and Gas Reservoir Geology and Exploitation; College of Chemistry and Chemical Engineering

Email: Lijingjing771216@gmail.com
中国, Chengdu, 610500; Chengdu, 610500

J. Li

College of Chemistry and Chemical Engineering

编辑信件的主要联系方式.
Email: Lijingjing771216@gmail.com
中国, Chengdu, 610500

L. Deng

College of Chemistry and Chemical Engineering

Email: Lijingjing771216@gmail.com
中国, Chengdu, 610500

G. Liang

College of Chemistry and Chemical Engineering

Email: Lijingjing771216@gmail.com
中国, Chengdu, 610500

补充文件

附件文件
动作
1. JATS XML

版权所有 © Pleiades Publishing, Ltd., 2017