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加氢试验装置反应器压差异常升高的原因分析及对策

韩龙年 王连英 杨国明 张海洪 朱元宝 陈禹霏

石油与天然气化工2023,Vol.52Issue(6):30-38,9.
石油与天然气化工2023,Vol.52Issue(6):30-38,9.DOI:10.3969/j.issn.1007-3426.2023.06.005

加氢试验装置反应器压差异常升高的原因分析及对策

Causes analysis and countermeasures for the abnormal rise of reactor pressure difference in hydrogenation test unit

韩龙年 1王连英 1杨国明 1张海洪 1朱元宝 1陈禹霏1

作者信息

  • 1. 中海油化工与新材料科学研究院
  • 折叠

摘要

Abstract

Objective The aim is to analyze the causes for the frequent abnormal rise of reactor pressure difference during hydrogenation evaluation test and put forward countermeasures.Methods X-ray fluorescence spectrometer(XRF),plasma spectrometer(ICP-OES),X-ray diffractometer(XRD)and other advanced instrument characterization and oil analysis methods were used to analyze the mud,raw oil and catalyst.Results (1)The top of the catalyst bed was full of mud,and the catalyst agglomerated in severe cases,which was the direct cause for the abnormal rise of pressure difference.(2)The mud was rich in elements such as Zn and Fe.(3)The pollution was more serious when the straight-run kerosene or diesel was stored in galvanized iron barrel,especially for the naphthenic straight-run diesel with high acid value and low viscosity,and the Zn mass fraction exceeded 100μg/g in short time,which was the fundamental cause for the abnormal rise of reactor pressure difference.Conclusions (1)For different petroleum fractions,suitable storage containers should be selected for sampling.(2)The storage container should be replaced in time and the independent hydrogenation protection section,demetallization section should be set for contaminated oil products during the evaluation test.(3)Special attention should be paid to the corrosion protection of acid-containing crude oil and its fractions during processing,especially naphthenic high-acid crude oil and its distillate.

关键词

加氢试验装置/反应器压差/异常升高/催化剂/结块

Key words

hydrogenation test unit/reactor pressure difference/abnormal rise/catalyst/agglomeration

引用本文复制引用

韩龙年,王连英,杨国明,张海洪,朱元宝,陈禹霏..加氢试验装置反应器压差异常升高的原因分析及对策[J].石油与天然气化工,2023,52(6):30-38,9.

石油与天然气化工

OA北大核心CSCD

1007-3426

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