摘要
清江石化采用MIP-CGP技术对重油催化裂化装置进行改造。改造后的标定结果表明:在不使用专用剂的情况下,100%负荷时MIP-CGP技术将催化裂化稳定汽油烯烃体积分数(荧光法)降至30%以下,下降了8%;汽油辛烷值RON和MON分别增加了1.52、0.70个单位,从而提高了汽油的抗爆指数;降低了汽油硫含量,汽油硫质量分数占原料硫质量分数的百分比至少下降了37.10%。在改善精制汽油性质的同时,还显著提高产品的总液体产品质量产率,明显减少干气质量产率与油浆质量产率。
Qingjiang petrochemical company of China petrochemical Co.,Ltd.(SINOPEC)adopted MIP-CGP process technology to transform the heavy oil catalytic unit.It started operation on September 29,2010 and operated normally for more than 4 months.The calibration results showed that the catalytic cracking stabilized gasoline olefin volume fraction(fluorescence method)can be reduced to less than 30%under 100%load of mip-cgp technology without the use of special agent,a decrease of 8%.The gasoline octane number RON and MON were increased by 1.52 and 0.7 units,respectively,which improved the knock resistance index of gasoline.The sulfur content of gasoline decreased by at least 37.10%.In addition to improving the properties of refined gasoline,the total liquid product yield of the product was significantly increased,and the dry gas yield and slurry yield were significantly reduced.
作者
李子国
LI Zi-guo(SINOPEC Qingjiang Petrochemical Co.,Ltd.,Jiangsu Huai'an 223002,China)
出处
《广州化工》
CAS
2021年第7期124-127,共4页
GuangZhou Chemical Industry