SCI和EI收录∣中国化工学会会刊

Chinese Journal of Chemical Engineering ›› 2019, Vol. 27 ›› Issue (10): 2498-2509.DOI: 10.1016/j.cjche.2019.01.014

• Process Systems Engineering and Process Safety • Previous Articles     Next Articles

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

Donghui Lü1, Yingjia Wang1, Lingjun Huang1, Di Zhang1, Guilian Liu1, Wei Li1, Peng Wang2   

  1. 1 School of Chemical Engineering and Technology, Xi'an Jiaotong University, Xi'an 710049, China;
    2 Hohhot Branch of PetroChina Pipeline Company, PetroChina, Hohhot 010000, China
  • Received:2018-09-15 Revised:2018-12-12 Online:2020-01-17 Published:2019-10-28
  • Contact: Guilian Liu
  • Supported by:
    Supported by the National Natural Science Foundation of China (21736008 and U1662126).

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

Donghui Lü1, Yingjia Wang1, Lingjun Huang1, Di Zhang1, Guilian Liu1, Wei Li1, Peng Wang2   

  1. 1 School of Chemical Engineering and Technology, Xi'an Jiaotong University, Xi'an 710049, China;
    2 Hohhot Branch of PetroChina Pipeline Company, PetroChina, Hohhot 010000, China
  • 通讯作者: Guilian Liu
  • 基金资助:
    Supported by the National Natural Science Foundation of China (21736008 and U1662126).

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 (T1) 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 T1 are linearly fitted. Based on this, the quantitative equation between HUA and T1 is derived, and corresponding diagram is constructed. The T1 corresponding the minimum hydrogen consumption is identified to be 345℃.

Key words: VGO hydrotreating, Reactors, Temperature, Hydrogen consumption

摘要: 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 (T1) 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 T1 are linearly fitted. Based on this, the quantitative equation between HUA and T1 is derived, and corresponding diagram is constructed. The T1 corresponding the minimum hydrogen consumption is identified to be 345℃.

关键词: VGO hydrotreating, Reactors, Temperature, Hydrogen consumption