首页|TH/FHUDS系列加氢催化剂级配技术的工业应用

TH/FHUDS系列加氢催化剂级配技术的工业应用

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针对某石化公司焦化汽柴油加氢装置掺炼催化柴油混合原料使得加氢脱硫难度增加,催化剂失活速率加快,催化剂寿命缩短等问题,开发出TH/FHUDS系列加氢催化剂级配技术,并与HPS/FHUDS加氢催化剂的工业应用进行对比.结果表明:与HPS/FHUDS加氢催化剂相比,TH/FHUDS加氢催化剂的加氢捕硅剂装填量减少 14.78 t,加氢精制催化剂装填量增加 42.27 t;在焦化汽柴油和催化柴油混合进料量为250 t/h,加氢保护反应器入口温度为 289℃,氢分压为 7.3 MPa,氢油体积比为 560,加氢主反应器平均反应温度为 364℃的条件下,能够稳定生产含硫量不大于 10 μg/g的超低硫柴油;后者的加氢脱硫、脱氮活性更高,芳烃饱和能力更强,精制柴油产品的含硫量降低 2.7 μg/g,含氮量降低 42.3 μg/g,多环芳烃质量分数降低 3.9 个百分点,十六烷值提高约 2 个单位.
Industrial application of TH/FHUDS series hydrogenation catalyst grading technology
The TH/FHUDS series hydrogenation catalyst grading technology had been developed to address issues such as increased difficulty in hy-drodesulfurization,accelerated catalyst deactivation rate,and shortened catalyst life caused by the blending of catalytic diesel as feedstock in the cok-ing gasoline/diesel hydrogenation unit of a petro-chemical company.The technology had been com-pared with the industrial application of HPS/FHUDS hydrogenation catalysts.The results showed that compared with HPS/FHUDS hydrogenation catalyst,the loading amount of hydrodesilication agent in TH/FHUDS hydrogenation catalyst decreased by 14.78 t,and the loading amount of hydrogenation refining catalyst increased by 42.27 t.Under the conditions of a mixed feed rate of 250 t/h of coking gasoline/diesel and catalytic diesel,an inlet temperature of 289℃for hydrogenation protection reactor,a hydrogen partial pressure of 7.3 MPa,a hydrogen oil volume ratio of 560,and an average reaction temperature of 364℃for the hydrogenation main reactor,produc-tion of ultra-low sulfur diesel with a sulfur content not exceeding 10 μg/g could be achieved stably.The latter had higher hydrogenation desulfurization and denitrification activity,stronger aromatic saturation ability,and the sulfur content of refined diesel products decreased by 2.7 μg/g,the nitrogen content decreased by 42.3 μg/g,the polycyclic aromatic hy-drocarbon mass fraction decreased by 3.9 percentage points,and cetane number increased by 2 units.

gasoline and diesel hydrogenationhydrodesilication agentcatalyst gradationcatalytic dieselrefined diesel

刘孝川、方友、苏灿、姜海波

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中海石油惠州石化有限公司 运行二部,广东 惠州 516086

中国石油抚顺石化公司 催化剂厂,辽宁 抚顺 113001

汽柴油加氢 加氢捕硅催化剂 催化剂级配 催化柴油 精制柴油

2024

石化技术与应用
兰州石化公司石油化工研究院

石化技术与应用

CSTPCD
影响因子:0.491
ISSN:1009-0045
年,卷(期):2024.42(5)