摘要
综述了催化裂化(Ⅲ)装置首次投产初期,分馏塔出现了顶循环油不稳定,轻柴油干点偏低等非正常工况的调整措施及取得的效果。
The adjustment measures and achieved results after fractionator appeared abnormal phenomenon of unstable topping cycle oil and lowly light diesel oil dry point at the initial stage of FCC （Ⅲ） workshop＇s production were described.
出处
《广州化工》
CAS
2015年第10期157-158,182,共3页
GuangZhou Chemical Industry
关键词
分馏塔
轻柴油干点
优化调整
fractionator
light diesel oil dry point
optimal adjustment
