Effect of vacuum gas oil hydrotreating reactor on multiple reactors and hydrogen network

Donghui Lü; Yingjia Wang; Lingjun Huang; Di Zhang; Guilian Liu; Wei Li; Peng Wang

doi:10.1016/j.cjche.2019.01.014

Your Location：

Home >

Browse articles >

Effect of vacuum gas oil hydrotreating reactor on multiple reactors and hydrogen network

Process Systems Engineering and Process Safety | Updated：2026-01-06

- Effect of vacuum gas oil hydrotreating reactor on multiple reactors and hydrogen network
- Chinese Journal of Chemical Engineering Vol. 27, Issue 10, Pages: 2498-2509(2019)
- Affiliations：
  
  1. School of Chemical Engineering and Technology, Xi'an Jiaotong University,Xi'an,China,710049
  2. Hohhot Branch of PetroChina Pipeline Company, PetroChina,Hohhot,China,010000
- Author bio：
- Funds：
- DOI：10.1016/j.cjche.2019.01.014
  CLC：
- Published：2019
- Accepted：
Scan QR Code
Donghui Lü, Yingjia Wang, Lingjun Huang, Di Zhang, Guilian Liu, Wei Li, Peng Wang. Effect of vacuum gas oil hydrotreating reactor on multiple reactors and hydrogen network[J]. Chinese Journal of Chemical Engineering, 2019, 27(10): 2498-2509.
DOI：

Donghui Lü, Yingjia Wang, Lingjun Huang, Di Zhang, Guilian Liu, Wei Li, Peng Wang. Effect of vacuum gas oil hydrotreating reactor on multiple reactors and hydrogen network[J]. Chinese Journal of Chemical Engineering, 2019, 27(10): 2498-2509. DOI： 10.1016/j.cjche.2019.01.014.

摘要

Abstract

The inlet temperature of the Vacuum Gas Oil (VGO) hydrotreating reactor of a refinery is analyzed with the integration of multiple series reactors and hydrogen network considered. The effect of the inlet temperature (

) on hydrogen sinks/sources and the product output is analyzed systematically based on the simulation of the series reactors

including VGO hydrotreating reactor

hydrocracking reactor

fluid catalytic cracking reactor and visbreaking reactor. The general relation between the Hydrogen Utility Adjustment (HUA) and multiple pairs of varying sinks and sources is deduced

and correlations between varying streams and

are linearly fitted. Based on this

the quantitative equation between HUA and

is derived

and corresponding diagram is constructed. The

corresponding the minimum hydrogen consumption is identified to be 345℃.

关键词

Keywords

references

Views

107

Downloads

CSCD

Alert me when the article has been cited

Submit

Tools

Publicity Resources

Numerical simulation of power and flow field characteristics of different spiral stirred reactors

Evaluation and application of kinetic models for Cu-catalyzed acetylene hydrochlorination

Flow characteristics simulation of spiral coil reactor used in the thermochemical energy storage system

High-gravity technology intensified Knoevenagel condensation-Michael addition polymerization of poly (ethylene glycol)-poly (n-butyl cyanoacrylate) for blood-brain barrier delivery

Effect of carboxymethyl cellulose on dissolution kinetics of carboxymethyl cellulose-sodium carbonate two-component tablet

Related Author

Zheng Wang

Bingxin Zhu

Zhiwei Zhang

Shuai Liu

Guobing Li

Fumin Wang

Xubin Zhang

Guodong Zhu

Related Institution

School of Chemical Engineering and Technology, Tianjin University

Department of Chemical Engineering, Tsinghua University

Mechanical Engineering College, Yangzhou University

School of Mechanical Engineering, Shanghai Institute of Technology

School of Mechanical and Power Engineering, Nanjing Tech University

⁰