Page 681 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
P. 681

Index                                              629

             Con trol valves, 90-96             Steam service, 426                  Lined,  171
             Dowtherrn  liquid, friction loss chart, 94   Type,400                  Turbine type,  169
             Dowtherrn vapor,  l 1  �           Valves,  parts,  412              Pumps, centrifugal system performance,  197
             Equivalent feel concept,  86      Pressure-vacuum relief,  466         Affinity laws, 201-203
             Equivalent feet,  non-viscous liquids,  89   Calculations, 469         Branch piping,  200
             Fittings,  71                      Emergency venting,  476-479         Calculations,  199
             Flashing liquids,  134-146         Equipment (valves), 468,  478, 480   Effects of performance changes, 201-203
             Flow coefficients,  Cv, for valves,  81   Fire exposure,  4  79        Head curve  for single pump,  198
             Friction loss,  68                 Free air,  469, 474                 Relations between head,  horsepower,
             Incompressible fluid, 71           Specification work sheet,  481         capacity and speed,  200
             Laminar flow,  77, 78, 86          Thermal outbreathing,  468, 469     Temperature rise 207-209
             Liquid lines,  chart, 92           Vacuum in  breathing,  468, 469,  475   Viscosity corrections,  203-207
             Long natural gas pipe lines,  120   Process check list,  35          Purging,  flare stack systems,  535
             Non-water liquids,  99            Process  design organization,  1, 2   Reciprocating pumps,  215-219
             Pipe,  71                          Calculations,  37-39                Flow  patterns,  219
             Resistance coefficient,  K,  71, 72, 73-77,   Costs,  43               Specification form, 219
                78-80                           Manhours,  40-43                  Relief areas,  437
             Resistance of fittings,  69, 70    Scope,  2                           External  fires,  451, 453
             Resistance of valves, 81          Process engineer, role, 3            Sizing,  434,  436
             Steam,  103                        Activity analysis,  36            Relief sizing, explosions gases/vapors,  505
             Sudden enlargement  zconuacuon. 70,  80   Estimated design manhours,  37   Deflagration venting,  506,  507
             Total  line, 64                    Time planning,  36                  High  strength venting,  508
             Two-phase flow,  124-127          Process planning,  scheduling,  flow sheet   Low strength venting,  508
             Vacuum lines,  128-134               design,  1                        NFPA Code, 506
             Velocities, 85, 89, 90            Process results,  mixing,  316,  323,  324   Venting (deflagration)  nomographs,  AP!,
             Velocities,  chart,  91           Process safety,  399                    509-512
             Velocity head, 71                 Properties of gases/vapors, 439      Venting,  dusts,  ( deflagration),
             Water flow calculations, 96       Pumping of liquids,  160                nomograph, API,  514-520
             Water flow,  table, 93, 97,  98   Pumps centrifugal,  161-164        Relief valves, 400
           Pressure level relationships,        AJ."\JSl Standards,  161            Code requirements, 415, 420
             Closing,  411                      Bearings,  168                      Installation,  422, 429-434
             Conform to Codes,  409, 410        Boiler feed water high pressure,  167   Safety-relief,  400
             Relieving,  411                    Brake  horsepower,  200           Relieving pressure,  411-417
             Resealing,  411                    Capacity-head ranges,  165        Resistance coefficient,  K,  (flow), 71, 72
             Rupture disks,  L.d O              Casing,  165                        Flow coefficient,  C,,, 81, 83
             Set pressur�  (relieving), 425, 455   Double suction,  166,  167       Pipe sizing,  83, 84, 86
             Simmer,  412                       Efficiency,  200                    Sudden contraction, 80
             Vacuum, 466                        High speed,  169                    Sudden enlargement,  80
             Valves, 409                        Illustrations,  161,  164           Tables/  charts, 73-  76,  77,  78-80
           Pressure levels chart,  53           Impellers,  164,  170               Valves,  81
             Reference, 56                      In parallel,  177,  178           Resistance,  equivalent feet,  design, 86-89
           Pressure piling,  explosion, 501     In series,  176,  178               Chart,  87,  88
           Pressure,                            Liquid horsepower,  200           Reynolds number.  55, 67
             Accumulation, 403                  Materials of construction,  211     Calculations,  68
             Levels, 409,  410                  Mixed flow,  169                    Chart,  110
             Operating,  408,  410              Multistage,  167                  Rotary pumps,  206
             Over,  403                         Operating curves,  180              Selection, 214-
             Relieving,  411                    Packing,  shaft,  170               Type,  213
           Pressure-relief terms/  definitions,  403   Performance curves,  180,  181, 182,  197   Roughness,  relative, 68
             External fires,  450               Rotative speed,  197                Chart,  68
             Relief areas,  437                 Seals, shaft,  168                Runaway reactions, 405
           Pressure-relieving devices,  399, 435-455   Selection guide,  178,  179   Runaway reactions,  DIERS,  521-523
             Balanced. valves, 400,  405, 407, 441   Single stage,  164           Rupture, disk,  401, 418, 435,  455
             Calculation of relief areas.  436, 440,   Single stage, single  impeller,  174   Burst pressure, 455
                441,449                         Specifications,  209                Calculations,  non-explosive, 455, 459
             Conventional valves, 400, 402, 407, 438   Stuffing box,  packing,  171   Code pressure levels,  410
             External  fires, 450,  453         System  performance,  197,  198     Effects of temperature,  458
             Genera, Code requirements,  412, 415,   Temperature rise, 207, 208,  209   Graphite,  418-'-120,  424
                420-425                         Turbine,  169                       Installation, ,122, 423
             Installation,  429-434             Turbine type performance,  178      Liquids, 462
             Materials of construction, valves, 402,   Vertical in-line,  165,  175   Low pressure,  418,  421
                404,405                         Vertical multistage,  168           Manufacturing range, 434,  456
             Pilot operated valves, 400,  406, 407   Vertical  propeller,  169      Metal, 411
             Rupture  disks,  401, 418, 451, 455   Viscosity correction, 203-207    Non-fire, 465
             Selection/application, 427,  434   Pumps  classes,  161                Quick opening,  414,  415
             Sizing,  436-441, 449, 434,  453   Basic pans,  centrifugal,  164      Reverse  buckling,  413
             Special.  401                      Design standardization,  161        Selection features, 434
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