摘要
以茂名石化加氢裂化尾油为原料,使用NKC-7型催化降凝催化剂,在固定床催化降凝装置上进行实验。在温度为340~400℃、空速为1~8h-1的条件下,考察了反应温度、空速对产品分布、凝点、收率的影响。结果表明:当温度为380℃、空速为2h-1时,得到较好的产品分布,润滑油基础油的凝点为-24℃,收率为61.4%。
Lube base oil were produced by catalytic dewaxing from hydrocracking tail oil of the Mao Ming Petrochemical Corporation in fixed catalytic bed reactor using NKC--7 as the dewaxing catalyst. The effects of reaction temperature (340- 400℃) and space velocity( 1-8 h^- 1) on the product distribution, solidifying point and liquid yield were studied. The results show that good product distribution and higher yield of lube base oil (61.4 % ) can be obtained at 380 ℃ and a space velocity of 2 h^-1 , the solidifying point of lube base oil can reach --24 ℃.
出处
《辽宁石油化工大学学报》
CAS
2011年第3期12-15,共4页
Journal of Liaoning Petrochemical University
关键词
催化降凝
加氢尾油
催化剂
润滑油基础油
Catalytic dewaxing
Hydrocraeking tail oils Catalyst
Lube base oil