摘要
在中国石油天然气股份有限公司吉林石化分公司0.6Mt/a加氢裂化装置扩大至0.9Mt/a的改造中,通过认真核算后确定新增的设备有:新氢压缩机、原料油泵及驱动原料泵的液力涡轮、脱硫化氢塔、脱硫化氢塔底重沸炉以及原料油缓冲罐等。设备的总体改动量不太大。从改造后标定结果看,改造达到了扩能要求,可增产乙烯装置原料0.21Mt。
The neatly-added new equipments for the capacity expansion revamping of hydrocracking unit from 12 000 b/d to 18 000 b/d in Refinery of Jilin Petrochemical Company include: fresh hydrogen compressor, feedstock pump, liquid turbine to drive feedstock pump, hydrogen sulfide absorbing tower, bottom reboiler in hydrogen sulfide absorbing tower and feedstock oil surge tank. Evaluation result shows that the revamp of unit has met capacity expansion requirement and the feedstock of ethylene unit can increased by 0. 21 Mt/a.
出处
《炼油技术与工程》
CAS
北大核心
2005年第4期23-25,共3页
Petroleum Refinery Engineering