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国产加氢催化剂HYT-6319及HC-185LT/HC-53LT的工业应用

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在中国石油广东石化公司 370 万t/a加氢裂化装置中,以中质减压蜡油和重芳烃的混合油(二者质量比 97∶3)为原料,使用经UOP公司授权由中国石油抚顺石化公司生产的加氢精制催化剂HYT-6319和加氢裂化催化剂HC-185 LT/HC-53 LT进行了工业应用,考察了催化剂运行情况、产品性质及其分布.结果表明:在催化剂运行中,一段精制、一段裂化、二段裂化反应器各床层入口平均温度依次比设计值低23.5~38.7,22.8~25.0,34.3~44.9℃,一段精制反应器床层平均温升比设计值低 10.1℃,一段裂化、二段裂化反应器床层平均温升比设计值分别高 3.4,3.6℃;柴油和航空煤油产品均满足国Ⅵ标准,重石脑油含硫(氮)量均小于 0.5 μg/g,是优质的重整装置原料,轻石脑油含硫量为 2.8 μg/g,是优质的乙烯裂解原料;主要产品重石脑油、航空煤油、轻石脑油、柴油的收率依次为 48.62%,25.28%,5.47%,14.14%,产品总收率为93.51%,比设计值高 0.04 个百分点.
Industrial application of domestic HYT-6319 and HC-185 LT/HC-53 LT hydrogenation catalysts
In the 3.70 Mt/a hydrocracking unit of Guangdong Petrochemical Company of PetroChina,a mixture of medium quality vacuum wax oil and heavy aromatics(with the mass ratio of 97∶3)was used as raw oil.The hydrofining catalyst HYT-6319 and hydrocracking catalyst HC-185 LT/HC-53 LT produced domestically by Fushun Petrochemical Company of PetroChina and authorized by UOP Company were used for industrial application.The catalysts operation,product properties and distribu-tion were investigated.The results showed that dur-ing the operation of the catalysts,the average tem-perature at the inlet of each bed layer in the first re-fining,first cracking,and second cracking reactors was lower than the design value by 23.5-38.7,22.8-25.0,34.3-44.9℃,respectively.The average tem-perature rise of the bed layer in the first refining re-actor was lower than the design value by 10.1℃,and the average temperature rise of the bed layer in the first cracking and second cracking reactors was higher than the design value by 3.4,3.6℃,respec-tively.Both diesel and aviation kerosene products met the nationalⅥstandard,and the sulfur(nitro-gen)content of heavy naphtha was less than 0.5 μg/g and being a high-quality raw material for reform-ing units.The sulfur content of light naphtha was 2.8 μg/g and being a high-quality ethylene crack-ing raw material.The yield of the main products in-cluding heavy naphtha,aviation kerosene,light naphtha,and diesel was 48.62%,25.28%,5.47%,and 14.14%,respectively.The total yield of prod-uct was 93.51%.It was higher than the design value by 0.04 percentage points.

hydrocrackinghydrorefiningcata-lystdiesel oilaviation keroseneheavy naphthayield

康海南、朱赫礼、罗毅

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中国石油广东石化公司 炼油生产三部,广东 揭阳 515299

加氢裂化 加氢精制 催化剂 柴油 航空煤油 重石脑油 收率

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(2)
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