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榆林减渣浆态床加氢中试试验研究

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以榆林减渣为原料,在浆态床加氢裂化装置进行中试试验.实验结果表明,在反应温度465 ℃、反应压力20 MPa、空速0.5 h-1、氢油比2 000 L/kg的条件下,榆林减渣加氢裂化反应性能和产物分布更优,>525 ℃的重组分和沥青质的转化率分别为84.69%和86.03%,气体产率和液收分别为7.57%和83.74%;采用Fe系催化剂等量替换赤泥催化剂,在抑制气体生成的同时提高了>525 ℃重组分、沥青质转化率及液体收率,分别提高了2.32%、2.67%和2.02%.
Research on pilot test of hydrogenation of slurry bed in Yulin
Using Yulin residue as the raw material,a pilot test was conducted in a slurry bed hydrocracking unit.The experimental results showed that under the conditions of reaction temperature 465 ℃,reaction pressure 20 MPa,space velocity 0.5 h-1,and hydrogen oil ratio 2,000 L/kg,the hydrocracking reaction performance and product distribution of Yulin residue were better.The conversion rates of>525 ℃ macromolecules and asphaltenes were 84.69%and 86.03%,respectively,and the gas yield and liquid yield were 7.57%and 83.74%.By replacing the red mud catalyst with a Fe-based catalyst in the same amount,the gas generation was inhibited while the conversion rates of>525 ℃ macromolecules,asphaltenes,and liquid yield were increased by 2.32%,2.67%,and 2.02%,respectively.

Slurry bedHydrocrackingCatalystYulin slag reductionhydrogen

高伟、问王伟、郭彦新、闻容基、汪亚斌、白罡

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陕西延长石油(集团)有限责任公司碳氢高效利用技术研究中心,陕西西安 710075

浆态床 加氢裂化 催化剂 榆林减渣

2024

炼油与化工
黑龙江省石油学会,大庆石化公司

炼油与化工

影响因子:0.185
ISSN:1671-4962
年,卷(期):2024.35(4)