摘要
以FCC汽油为原料,在中型试验装置上考察230~400℃范围内硫化温度对MoCo/Al2O3催化剂加氢脱硫率及烯烃加氢饱和率、产品辛烷值损失的影响。结果表明:在反应温度260℃下,随着硫化温度的提高,加氢脱硫率由84.4%逐步提高到91.1%;在反应温度280℃下,加氢脱硫率均可维持在96.0%以上,受硫化温度的影响较小。在上述两种情况下,250℃硫化时催化剂的烯烃加氢饱和率最低,辛烷值损失最小。表明250℃硫化时催化剂的加氢脱硫选择性最好。MoCo/Al2O3催化剂在250℃下硫化充分且碳含量较少是其FCC汽油加氢脱硫选择性最好的原因。
The effect of presulfurization temperature (230--400℃) of MoCo/Al2O3 catalyst on its selective hydrodesulfurization (HDS) performance, such as HDS rate, hydro-saturation (HYD) rate and gasoline octane (RON) loss,was studied on a pilot plant unit using full range FCC gasoline as feed. The test results indicated that under reaction temperature of 260℃, with the increase of presulfurization temperature,the HDS rates of these catalysts increased from 84.4% to 91. 1%; under reaction tempera- ture of 280℃ ,the HDS rates of these catalysts were all over 96.0%,presulfurization temperature had less influence. However,in these two eases,MoCo/Al2O3 catalyst sulfurized at 250℃ exhibited the minimum HYD rate and gasoline RON loss, which indicated said catalyst possessed the best HDS selectivity. It was found that MoCo/Al2O3 eatalyst could be well sulfurized at 250℃ and with less coke deposit, which would be favorable to provide good HDS selectivity when treating FCC gasoline.
出处
《石油炼制与化工》
CAS
CSCD
北大核心
2011年第12期33-35,共3页
Petroleum Processing and Petrochemicals
基金
中国石油化工股份有限公司"十条龙"重大科技攻关项目(010803)