Page 11 - Pipeline Rules of Thumb Handbook
P. 11

Examples of pressure drop calculations for rubber     14: Pumps, 399
            hose  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 341
         Typical formulas used for calculating pressure drop   Centrifugal pumps  . . . . . . . . . . . . . . . . . . . . . . . . . . . 400
            and flow rates for pipelines  . . . . . . . . . . . . . . . . . . 341  Speed torque calculation  . . . . . . . . . . . . . . . . . . . . . . 412
         Hydraulic gradients  . . . . . . . . . . . . . . . . . . . . . . . . . . 343  Pulsation Control for Reciprocating
         Equivalent lengths  . . . . . . . . . . . . . . . . . . . . . . . . . . . 346  Pumps  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 413
         Series systems  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 347
         Looped systems  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 348  Key Centrifugal Pump Parameters and
         Calculate pressure loss in annular sections  . . . . . . . . . 349  How They Impact Your Applications—
         Calculate pressure and temperature loss for viscous      Part 1  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 421
            crudes ≥1,000cP  . . . . . . . . . . . . . . . . . . . . . . . . . . 349
         Determine batch injection rate as per enclosure . . . . . 352  Key Centrifugal Pump Parameters and
                                                                  How They Impact Your Applications—
         Pressure Loss through Valves and                         Part 2  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 426
            Fittings  . . . . . . . . . . . . . . . . . . . . . . . . . . . . 353
                                                               Estimate the discharge of a centrifugal pump at
         Representative resistance coefficients (K) for valves     various speeds  . . . . . . . . . . . . . . . . . . . . . . . . . . . . 431
            and fittings  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 353  How to estimate the head for an average centrifugal
         Nomograph for calculating Reynolds number for flow        pump  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 431
            of liquids and friction factor for clean steel and   Find the capacity of reciprocating pump  . . . . . . . . . . 432
            wrought iron pipe  . . . . . . . . . . . . . . . . . . . . . . . . . 359  How to estimate the horsepower required to pump
         Nomograph for calculating pressure drop of liquids in    at a given rate at a desired discharge pressure  . . . . 432
            lines for turbulent flow  . . . . . . . . . . . . . . . . . . . . . 361  Nomograph for determining reciprocating pump
                                                                  capacity . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 432
         Drag-Reducing Agents  . . . . . . . . . . . . . . . . 365  Nomograph for determining specific speed of
                                                                  pumps . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 434
         The basics of drag reduction  . . . . . . . . . . . . . . . . . . . 365
                                                               Nomograph for determining horsepower requirement
         How drag-reducing agents can outweigh looping or
                                                                  of pumps . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 435
            boosting  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 370
                                                               How to select motors for field gathering pumps  . . . . . 435
         How active, passive drag affect DRA injections  . . . . . 376
                                                               Reciprocating pumps  . . . . . . . . . . . . . . . . . . . . . . . . . 436
         How to estimate the rate of liquid discharge from a
                                                               Understanding the basics of rotary screw pumps  . . . . 445
            pipe  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 382
         Predict subsurface temperature ranges . . . . . . . . . . . . 382
         Sizing pipelines for water flow  . . . . . . . . . . . . . . . . . . 383  15: Measurement, 451
         How approximate throughput of a line can be
            estimated from pipe size  . . . . . . . . . . . . . . . . . . . . 384  Pipeline flow measurement—the new influences  . . . . 452
         Gauge liquid flow where no weir or meter is            Liquid measurement orifice plate flange taps  . . . . . . . 455
            available  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 384  Mass measurement light hydrocarbons . . . . . . . . . . . . 459
         Estimate crude gathering line throughput for a given   Pipeline measurement of supercritical carbon
            pipe diameter  . . . . . . . . . . . . . . . . . . . . . . . . . . . . 384  dioxide  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 460
         How to determine head loss due to friction in         Gas Measurement  . . . . . . . . . . . . . . . . . . . . 466
            ordinary iron pipeline carrying clear water . . . . . . . 384
         How to size lines, estimate pressure drop and         Master meter proving orifice meters in dense phase
            optimum station spacing for crude systems  . . . . . . 385  ethylene  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 466
         Estimate the optimum working pressures in crude oil   Gas or vapor flow measurement—orifice plate flange
            transmission lines  . . . . . . . . . . . . . . . . . . . . . . . . . 385  taps . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 473
         How to size crude and products lines for capacity     Properties of gas and vapors . . . . . . . . . . . . . . . . . . . . 477
            increases  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 386  Determine required orifice diameter for any required
         How to determine the maximum surge pressure in           differential when the present orifice and differential
            liquid-filled pipeline when a main valve is closed     are known in gas measurement  . . . . . . . . . . . . . . . 482
            suddenly  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 386  Estimate the temperature drop across a regulator  . . . 483
         What is the hydrostatic pressure due to a column of   Estimate natural gas flow rates . . . . . . . . . . . . . . . . . . 483
            oil H feet in height?  . . . . . . . . . . . . . . . . . . . . . . . 386  How to estimate the average pressure differential
         Transient pressure analysis . . . . . . . . . . . . . . . . . . . . . 387  on the remaining meter runs of a parallel system
         Tank farm line sizing  . . . . . . . . . . . . . . . . . . . . . . . . . 396  when one or more runs are shut off . . . . . . . . . . . . 484

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