摘要
利用金属浴加热和水冷的办法对南京炼油厂焦化循环渣油进行急剧升温和降温,在低温(400℃～440℃)恒温和高温(460℃～500℃)非恒温的7个不同温度下,进行了不同反应时间条件下的热裂解反应动力学规律的研究(2.4.5)。文中给出了南京焦化循环渣油热转化反应动力学模型。
The kinetics of thermal-conversion of the recycle residue in the delayed coker of Nanjing refinery was experimentally studied in the temperature range of 400～500℃ by using a metal bath reactor, kinetic models were obtained. Experimental results provide the basis for the study of tubular heater. The method at data treatmant for kinetic study is given.
出处
《石油学报（石油加工）》
EI
CAS
CSCD
北大核心
1995年第3期7-12,共6页
Acta Petrolei Sinica(Petroleum Processing Section)
基金
国家"八五"攻关课题
关键词
渣油
热转化
动力学
热裂化
residue, thermal conversion, kinetics
