Safety devices for protection against excessive pressure — Sizing of safety valves and connected inlet and outlet lines for gas/liquid two- phase flow

[1]  Joseph C. Leung,et al.  Two-phase flow discharge in nozzles and pipes — a unified approach☆ , 1990 .

[2]  Robert E. Henry,et al.  The Two-Phase Critical Flow of One-Component Mixtures in Nozzles, Orifices, and Short Tubes , 1971 .

[3]  Api Standard.  Sizing, Selection, and Installation of Pressure-relieving Devices in Refineries , 2008 .

[4]  Frank P. Lees,et al.  Loss Prevention In The Process Industries , 1980 .

[5]  Ron Darby,et al.  On two-phase frozen and flashing flows in safety relief valuesRecommended calculation method and the proper use of the discharge coefficient , 2004 .

[6]  L. Friedel,et al.  Pressure relief system design for vapour or two-phase flow? , 1994 .

[7]  Joseph C. Leung.  Venting of runaway reactions with gas generation , 1992 .

[8]  Ralf Diener,et al.  Sizing of throttling device for gas/liquid two‐phase flow part 1: Safety valves , 2004 .

[9]  Charles M. Sheppard.  DIERS churn—turbulent disengagement correlation extended to horizontal cylinders and spheres , 1993 .

[10]  J. B. Fussell.  Fault tree analysis: concepts and techniques , 1976 .

[11]  Api Recommended Practice.  Guide for Pressure-Relieving and Depressuring Systems , 1997 .

[13]  Harold G. Fisher,et al.  Protection of storage tanks from two‐phase flow due to fire exposure , 1995 .

[14]  Richard Rogers,et al.  Chemical Reaction Hazards , 1997 .

[15]  Jasbir Singh.  Vent sizing for gas-generating runaway reactions , 1994 .

[16]  G. A. Melhem,et al.  International symposium on runaway reactions and pressure relief design , 1995 .

[17]  Hans K. Fauske,et al.  Emergency relief vent sizing for fire emergencies involving liquid‐filled atmospheric storage vessels , 1986 .