选择质量分数ｗ（苯）１２２８％，ｗ（甲苯）３３２％，ｗ（芳烃）１５６％的６＃抽提溶剂油为原料，应用镍铝催化剂在１０ｍＬ高压加氢固定床微反气相色谱联合装置上进行催化加氢脱芳烃的研究，考察了不同操作条件下６＃抽提溶剂油催化加氢脱芳烃的效果。在反应压力０５ＭＰａ，氢油体积比７０∶１，反应温度１３０℃，空速１０ｈ－１的条件下，６＃抽提溶剂油催化加氢脱芳烃的效果较好，加氢后油中ｗ（总芳烃）可降至００５％，符合中国石油天然气总公司科技局提出的油中ｗ（芳烃）不大于０１０％的要求。 Six (6) extraction solvent oils with w (benzene) 1228%, w (toluene) 332% and w (aromatic) 156% were used as raw materials. Micro anti-GC combined catalytic hydrogenation of dearomatization on the study under different operating conditions 6 # solvent oil catalytic hydrodearomatization effect. Under the conditions of reaction pressure of 0.5MPa, volume ratio of hydrogen to oil of 70:1, reaction temperature of 130 ℃ and space velocity of 10h-1, the catalytic effect of 6 # solvent oil on hydrodearomatization is better. After hydrogenation Oil w (total aromatics) can be reduced to 0  05%, in line with the China National Petroleum Corporation Science and Technology Bureau proposed oil w (aromatics) is not more than 0  10% of the requirements.