Page 10 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
P. 10

Estimating Blast Pressures and Destruction, 50 l; Blast Scaling,   Stainless  Steel  Pipe  Data,  588;  A-16:  Properties  of Pipe,  589:
                503;  Example 7-l5:  Blast Scaling,  503;  Example 7-16:  Estimat-   A-17:  Equation of  Pipes, 598; A-18: Circumferences and Areas of
                ing  Explosion  Damage,  504;  Explosion  Venting  for   Circles,  599;  A-19:  Capacities  of Cylinders  and  Spheres,  605;
                Gases/Vapors  (Not Dusts), 504;  Liquid  Mist  Explosions,  505;   A-20:  Tank  Capacities,  Horizontal  Cylindrical=-Contents  of
                Relief Sizing:  Explosions  of Gases  and  Vapors,  505;  Vent  or   Tanks with Flat Ends When  Filled  to Various Depths,  609; A-21:
                Relief Area  Calculation  for Venting  of Deflagrations  in  Low-   Tank Capacities, Horizontal Cylindrical-Contents of Standard
                Strength  Enclosures, 507;  Example  7-17:  Low Strength  Enclo-   Dished  Heads  When  Filled  to Various  Depths,  609;  A-22:  Mis-
                sure Venting, 508; High Strength Enclosures for Deflagrations,   cellaneous Formulas,  610; A-23:  Decimal  Equivalents in Inches,
                508;  Determination  of  Relief  Areas  for  Deflagrations  of   Feet and Millimeters, 611; A-24:  Properties of the Circle, Area of
                Cases/Vapors/Mists  in  High  Strength  Enclosures,  508;  Dust   Plane Figures,  and Volume ofa Wedge,  612; A-24  (continued):
                Explosions,  513;  Example  7-18:  Use of the Dust Nomographs,   Trigonometric  Formulas  and  Properties  of Sections,  613;  A-24
                514; Unconfined Vapor Cloud Explosions,  520; Effects of Vent-   (continued):  Properties  of  Sections,  614;  A-25:  Wind  Chill
                ing  Ducts,  521:  Runaway  Reactions;  DlERS.  521;  Flares/Flare   Equivalent Temperatures on Exposed Flesh at Varying Velocity,
                Stacks,  523; Flares,  528;  Example 7-19:  Purge Vessel by Pressur-   617;  A-26:  Impurities  in 'Water,  617;  A-27:  Water Analysis  Con-
                ization, 535;  Static  Electricity,  535.            versions for Units  Employed:  Equivalents,  618;  A-28:  Parts  Per
                                                                     Million to Grains Per U.S.  Gallon,  618;  A-9:  Formulas,  Molecu-
            Appendix                                       54  7     lar and Equivalent Weighlf, and Conversion Factors to CaCo 3  of
                                                                     Substances  Frequently  Appearing  in  the  Chemistry  of Water
                A-1: Alphabetical Conversion Factors, 547; A-2:  Physical Proper-   Softening, 619; A-30: Grains Per U.S. Gallons-Pounds Per 1000
                ty  Conversion  Factors,  571; A-3:  Synchronous Speeds,  574; A-4:   Gallons, 621; A-31: Pares Per Million-Pounds Per 1000 Gallons,
                Conversion  Factors.  574;  A-5:  Temperature  Conversion,  577;   621; A-32:  Coagulant,  Acid,  and  Sulfate-]  ppm  Equivalents,
                A-6:  Altitude and  Atmospheric Pressures,  578;  A-7:  Vapor  Pres-   621; A-33:  Alkali and Lime-1  ppm Equivalents,  622;  A-34: Sul-
                sure Curves, 579; A-8:  Pressure Conversion Chart, 580; A-9: Vac-
                uum  Conversion,  581;  A-10:  Decimal  and  Millimeter  Equiva-   furic,  Hydrochloric Acid  Equivalent,  622;  A-35:  ASME  Flanged
                lents  of Fractions,  .582;  A-11: Particle Size  Measurement,  582;   and Dished Heads IDD Chart,  623; A-35  (continued):  Elliptical
                                                                     Heads,  624; A-35  (continued): 80-10 Heads,  625.
                A-12:  Viscosity  Conversions,  583;  A-13:  Viscosity  Conversion,
                584;  A-11:  Commercial  Wrought  Steel  Pipe  Data,  585;  A-15:
                                                                 Index                                          626

















































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