1.论文 (1)New Visual Test Method for the Toluene Insolubles in OilProducts,[J].Energy & Fuels, 2020, 34, 2, 1447-1452. (2)延迟焦化加热炉炉管焦组成与成因分析[J].石油大学学报(自然科学版),2020.44(1):180-184 . (3)J. Yang, G. Shen, P. Lin, W. Wei, C. Zhang, J. Xiao(*), KineticModel for the Deep-Severity Thermal Reaction in the Coke Drum ofDelayed Coking [J]. Energy & Fuels, 2017. (4)J. Yang, G. Shen, P. Lin, W. Wei, C. Zhang, J. Xiao(*), KineticModel for the Deep-Severity Thermal Reaction in the Coke Drum ofDelayed Coking [J]. Energy & Fuels, 2017. (5)J. Yang, C. Liu, S. Li, B. Sun, J. Xiao(*),Y. Jin. A new pressuredrop model of gas–liquid cyclone with innovative operation mode[J]. Chemical Engineering and Processing: Process Intensification,2015, 95:256-266. (6)J. Yang, X. Zhang, G. Shen, J. Xiao(*),Y. Jin. Modeling the MeanResidence Time of Liquid Phase in the Gas–Liquid Cyclone [J].Industrial & Engineering Chemistry Research, 2015,54(43):10885-10892. (7)杨军卫,赵加民,王建军,肖家治,金有海.气液旋流器内液相平均停留时间[J].化工学报,2015. (8)J. Yang, G. Shen, L. Wang, J. Xiao(*),C. Yang. Practical Model forthe Induction Period of Heavy Oil during Thermal Reaction [J].Energy & Fuels, 2013, 27(4): 2068-2072. (9)J. W. Yang, N. N. Tai, L. J. Wang, J. Z. Xiao(*),C. H. Yang.Numerical Simulation of the Flue Gas and Process Side of CokingFurnaces [J].Industrial & engineering chemistry research,2012, 51(47):15440-15447. (10)J. W. Yang, D. X. Chen, G. P. Shen, J. Z. Xiao(*),C. H. Yang.Narrow Fraction Model with Secondary Cracking for Low-SeverityThermal Cracking of Heavy Oil [J]. Energy & Fuels, 2012,26(6):3628-3633. 2.专利 (1)测定气液旋流液相停留时间分布的装置和方法,中国,ZL2015107123312。 (2)圆筒型管式加热炉,中国,ZL201810384804.4。 (3)立管方箱炉,中国,ZL201820607259.6 (4)圆筒型管式加热炉,中国,ZL201821686741.X (5)检测装置和悬浮液中的颗粒检测方法,中国,ZL201910330832.2 (6)一种改善热强度分布的加氢炉,中国,ZL20142 0455022.2。 (7)一种延迟焦化加热炉,中国,CN201010554752.4。 (8)对称双阶梯管式辐射炉,中国,ZL2011 20503562.X。 (9)加热炉倒梯形贴墙燃烧器,中国,ZL2010 2 0293852.1。 (10)一种便于现场观火和调火的管式加热炉,中国,ZL2010 20293836.2。 |