摘要
本文根据20万t/a DCC裂解石脑油加氢装置一反检修检查情况并结合装置运行工况,分析认为该装置一反压降大的主要原因为:一反催化剂初始装填方案不合理,上部床层空高过大;DCC石脑油中二烯烃等不饱和烃含量较高,易发生缩合反应生成焦质;DCC石脑油在罐区储存时间长且氮封效果不好;装置晃电、氢气压力波动等加剧了系统压降增涨。同时还提出了预防一反压降增大的措施及建议。
This paper according to the 20 million t / a DCC naphtha hydrogenation unit is opposite to the maintenance inspection combined with device operating conditions,analysis the device a anti drop the main reason for unreasonable against initial catalyst loading scheme,at the top of the bed layer height; DCC naphtha diene hydrocarbon content of unsaturated hydrocarbon is high,prone to condensation reaction to produce coke quality; DCC naphtha in tank farm storage for a long time and nitrogen sealing effect is not good; device Akira electricity,hydrogen pressure fluctuation etc. exacerbates the system pressure drop increase. At the same time,it puts forward some measures and suggestions to prevent the increase of pressure drop.
出处
《山东化工》
CAS
2016年第21期121-122,共2页
Shandong Chemical Industry