广州化工
廣州化工
엄주화공
GUANGZHOU CHEMICAL INDUSTRY AND TECHNOLOGY
2015年
10期
157-158,182
,共3页
分馏塔%轻柴油干点%优化调整
分餾塔%輕柴油榦點%優化調整
분류탑%경시유간점%우화조정
fractionator%light diesel oil dry point%optimal adjustment
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。
綜述瞭催化裂化( III)裝置首次投產初期，分餾塔齣現瞭頂循環油不穩定，輕柴油榦點偏低等非正常工況的調整措施及取得的效果。
종술료최화열화( III)장치수차투산초기，분류탑출현료정순배유불은정，경시유간점편저등비정상공황적조정조시급취득적효과。
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.
