| [1]蔡奇, 杨玉旺, 吴同旭, 等.对催化剂及其丙烷脱氢性能的影响[J].石油炼制与化工, 2016, 47(3):72-76[2]刘昌呈, 王春明, 马爱增.工艺条件对--催化剂丙烷脱氢性能的影响[J].石油炼制与化工, 2013, 44(4):34-38[3]Gascon J, Tellez C, Herguido J, et al.Propane dehydrogenation over a Cr2O3Al2O3 catalyst: transient kinetic modeling of propene and coke formation[J].Applied Catalysis A: General, 2003, 248(1):105-116[4]李庆, 隋志军, 朱贻安, 等.催化丙烷脱氢过程中结焦反应的粒径效应与的作用[J].化工学报, 2013, 64(2):524-531[5] 赵万恒.低碳烷烃脱氢技术评述[J].化工设计, 2000, 67(3):11-13[6] 张海娟, 高杰, 张浩楠, 等.低碳烷烃深加工制烯烃技术的研究进展[J]. [J].石油化工, 2016, 77(12):1411-1419[7] Vernikovskaya N V, Savin I G, Kashkin V N, et al.Dehydrogenation of propane–isobutane mixture in a fluidized bed reactor over Cr2O3/Al2O3 catalyst: Experimental studies and mathematical modelling[J].Chemical Engineering Journal, 2011, 176(1):158-164[8] 李洪钟, 郭慕孙.回眸与展望流态化科学与技术[J]. [J].化工学报, 2013, 64(1):52-62[9]杨朝合, 杜玉朋, 赵辉.催化裂化提升管反应器流动反应耦合模型研究进展[J].化工进展, 2015, 34(3):608-616[10] Wang W, Lu B, Zhang N, et al.A review of multiscale CFD for gas–solid CFB modeling[J]. [J].International Journal of Multiphase Flow, 2010, 36:109-118[11] Wang J, Liu Y.EMMS-based eulerian simulation on the hydrodynamics of a bubbling fluidized bed with FCC particles[J]. [J].Powder Technology, 2010, 197:241-246[12] Lu B, Luo H, Li H, et al.Speeding up CFD simulation of fluidized bed reactor for MTO by coupling CRE model[J]. [J].Chemical Engineering Science, 2016, 143:341-350[13] Shi Z, Wang W, Li J.A bubble-based EMMS model for gas–solid bubbling fluidization[J]. [J].Chemical Engineering Science, 2011, 66:5541-5555 |
京公网安备 11010802027553号
