降膜式冷凝蒸发器的调研
摘要
介绍了浸浴式冷凝蒸发器和降膜式冷凝蒸发器的工作原理以及两者间的区别,展示了一些国外大型空分公司设计的液体分布器结构形式,并阐述了国内一些学者在换热器降膜传热和物流分配研究领域的成果。
引文
[1]毛绍融,朱朔元,周智勇,等.大型空分设备技术现状及进展[J].深冷技术,2009,1:26-31.
[2]毛央平,柳红霞.大型空分设备冷凝蒸发器结构研究[J].深冷技术,2009,3:18-20.
[3]SCHMIDT W.ASU condenser/reboiler safety.Present at European Industrial Gas Assocation Production Safety Seminar[C].2006.
[4]马大方.武钢60000m3/h制氧机流程与主冷型式的选择[J].深冷技术,2003,5:1-10.
[5]林青松.60000m3/h制氧机膜式主冷安全性分析及安全措施[J].安全技术,2004,5:39-42.
[6]陈智浩.一氧化二氮的积聚和膜式冷凝蒸发器[J].深冷技术,1999,6:45-47.
[7]SCHMID W P,WINEGARDNER K S,DENNEHY M,et al.Safe design and operation of a cryogenic air separation unit[J].Process Safety Progress,2001,20(4):269-279.
[8]HARDEVELD R V,GROENEVELDA M J,LEHMAN J Y,et al.Investigation of an air separation unit explosion[J].Journal of Loss Prevention in the Process Industries,2001,14(3):167-180.
[9]PETIT P,GRENIER M,DESCHAMPS J F.Process and Services for Vaporizing a Liquid by Heat Exchange with a Second Fluid and Their Application in a Air Distillation Istallation[P].US,4599097,1986-06-08.
[10]SEIICHI S,HIDEYUKI H,JUNICHI O.Downflow Liquid Film Type Condemser Evaporator[P].US,6338384,2002-01-15.
[11]SRINIVASAN V,MICHAEL J L,JOHN H Z.Downflow Plate and Fin Heat Exchanger for Cryogenic Rectification[P].US,5438836,1995-08-08.
[12]SWAMINATHAN S,BENNETT D L,HERRON D M,et al.Boiling Process and a Heat exchanger for Use in the Process[P].US,5122174,1992-01-16.
[13]ZHOU Y,YU J L,LI Y Z.A study on flow and heat transfer characteristics for saturated falling-film evaporation of liquid oxygen in a vertical channel[J].International Journal of Heat and Mass Transfer.2012,55:7218-7222.
[14]焦安军,厉彦忠,张瑞,等.封头结构对板翅式换热器物流分配不均匀性的影响[J].化学工程,2003,7:907-912.
[15]刘玉峰,童一峻,任海刚,等.高雷诺数竖壁降膜流动特性的数值研究[J].红外技术,2010,32(10):567-571.
[16]朱冬生,张景卫,吴治将,等.板式蒸发式冷凝器两相降膜流动CFD模拟及传热研究[J].华南理工大学学报,2008,36(7):6-10.
[2]毛央平,柳红霞.大型空分设备冷凝蒸发器结构研究[J].深冷技术,2009,3:18-20.
[3]SCHMIDT W.ASU condenser/reboiler safety.Present at European Industrial Gas Assocation Production Safety Seminar[C].2006.
[4]马大方.武钢60000m3/h制氧机流程与主冷型式的选择[J].深冷技术,2003,5:1-10.
[5]林青松.60000m3/h制氧机膜式主冷安全性分析及安全措施[J].安全技术,2004,5:39-42.
[6]陈智浩.一氧化二氮的积聚和膜式冷凝蒸发器[J].深冷技术,1999,6:45-47.
[7]SCHMID W P,WINEGARDNER K S,DENNEHY M,et al.Safe design and operation of a cryogenic air separation unit[J].Process Safety Progress,2001,20(4):269-279.
[8]HARDEVELD R V,GROENEVELDA M J,LEHMAN J Y,et al.Investigation of an air separation unit explosion[J].Journal of Loss Prevention in the Process Industries,2001,14(3):167-180.
[9]PETIT P,GRENIER M,DESCHAMPS J F.Process and Services for Vaporizing a Liquid by Heat Exchange with a Second Fluid and Their Application in a Air Distillation Istallation[P].US,4599097,1986-06-08.
[10]SEIICHI S,HIDEYUKI H,JUNICHI O.Downflow Liquid Film Type Condemser Evaporator[P].US,6338384,2002-01-15.
[11]SRINIVASAN V,MICHAEL J L,JOHN H Z.Downflow Plate and Fin Heat Exchanger for Cryogenic Rectification[P].US,5438836,1995-08-08.
[12]SWAMINATHAN S,BENNETT D L,HERRON D M,et al.Boiling Process and a Heat exchanger for Use in the Process[P].US,5122174,1992-01-16.
[13]ZHOU Y,YU J L,LI Y Z.A study on flow and heat transfer characteristics for saturated falling-film evaporation of liquid oxygen in a vertical channel[J].International Journal of Heat and Mass Transfer.2012,55:7218-7222.
[14]焦安军,厉彦忠,张瑞,等.封头结构对板翅式换热器物流分配不均匀性的影响[J].化学工程,2003,7:907-912.
[15]刘玉峰,童一峻,任海刚,等.高雷诺数竖壁降膜流动特性的数值研究[J].红外技术,2010,32(10):567-571.
[16]朱冬生,张景卫,吴治将,等.板式蒸发式冷凝器两相降膜流动CFD模拟及传热研究[J].华南理工大学学报,2008,36(7):6-10.