摘要
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％.
Abstract
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.
维普
万方数据