摘要
本文提出了渣油气化炉的数学模型,计算值与引进装置测定值吻合良好.预测了工艺条件变化对反应结果的影响.
The mathematical model for gasifier of redidual oil has been presented in this paper. The results show that the calculated values agree very well with the design data and operation data. The effects of operation conditions on results of chemical reaction have been predicted.
出处
《石油学报（石油加工）》
EI
CAS
CSCD
北大核心
1993年第3期69-77,共9页
Acta Petrolei Sinica(Petroleum Processing Section)
