Energy saving in a crude distillation unit by a preflash implementation
暂无分享,去创建一个
[1] Miguel J. Bagajewicz,et al. Rigorous Procedure for the Design of Conventional Atmospheric Crude Fractionation Units. Part I: Targeting , 2001 .
[2] R. Yahyaabad. Solving hydraulic problems in crude preheat train networks , 2005 .
[3] D. S. J. Jones. Elements of petroleum processing , 1995 .
[4] G. R. Martin,et al. Consider comprehensive CPD efforts to cut costs , 2002 .
[5] Miguel J. Bagajewicz,et al. Design of Crude Distillation Plants with Vacuum Units. I. Targeting , 2002 .
[6] G. Mansoori,et al. Continuous thermodynamics of petroleum fluids fractions , 2001 .
[7] R Yahyaabadi. Solving hydraulic problems in crude preheat train networks - Heat transfer and hydraulic problems need to be considered simultaneously , 2005 .
[8] H. M. Feintuch,et al. A preflash drum can conserve energy in a crude preheat train , 1985 .
[9] Miguel J. Bagajewicz,et al. Design of Crude Fractionation Units with Preflashing or Prefractionation: Energy Targeting , 2002 .
[10] R. Yahyaabadi. Rethink placement of preflash drum in crude preheat train network , 2006 .
[11] C. H. Whitson,et al. Characterizing hydrocarbon plus fractions , 1983 .
[12] S. W. Golden. Prevent preflash drum foaming , 1997 .
[13] B. Linnhoff,et al. The pinch design method for heat exchanger networks , 1983 .
[14] Mohammad R. Riazi,et al. A Continuous Model for C7+ Fraction Characterization of Petroleum Fluids , 1997 .
[15] Srbislav Genić,et al. Use a new approach to find Murphree tray efficiency , 1996 .