Page 73 - Handbook Of Multiphase Flow Assurance
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68                             4.  Hydraulic and thermal analysis

                                                   Introduction

                   Hydraulic analysis is used to calculate and optimize pressure loss, holdup accumulation,
                 vibration, water hammer and surge exceeding normal operating parameters during steady
                 and transient flow operations. Sensitivity to the amounts of produced water should include
                 an assumption for planned and deferred water injection for pressure support, based on reser-
                 voir simulation production profiles.
                   Thermal analysis predicts the temperature changes in the produced fluid and in the pro-
                 ducton system as heat is lost to ambient cooling or to JT expansion in multiphase flow or
                 gained from JT heating in supercritical (dense phase) fluids. Thermal analysis in wells is also
                 related to mechanical integrity if annular spaces are filled with fluids with low compressibility.
                   Both thermal and hydraulic analysis are performed simultaneously, coupled through location
                 in the system. Fluid properties depend both on temperature and pressure, and proper fluid char-
                 acteristics and phase transitions rely on accurate calculation of both temperature and pressure.
                   Hydraulic analysis results are supplied to operability design analysis which aims to ensure
                 that temperature, pressure and flow are within normal operating limits for the production
                 system at any stage in field development life.
                   Flow lines from trees to manifolds and from manifolds to hubs are usually routed pre-
                 dominantly uphill to minimize pressure losses due to terrain liquids holdup in low spots, in
                 order to maximize overall fluid recovery by limiting backpressure on wells, and also to avoid
                 slugging induced by liquid accumulation in low spots and to enable uniform subsea chemical
                 distribution in produced fluid, and to reduce fatigue from cyclic slug impacts on pipe elbows
                 at bends and crossings.
                   Detailed field layout should ensure that both production and chemical injection systems
                 can operate with acceptable pressure drop and chemical stability in subsurface, subsea, top-
                 sides and export systems conditions.
                   Single line tieback concepts are economically attractive and may be considered for early
                 production systems if reliable ways to mitigate the risk of solids restriction are in place.


                                Hydraulic restrictions boundaries and management

                   Besides the regular solid blockages which derive from a phase transition such as solid
                 crystallization of normal paraffins as wax there also may be hydraulic restrictions in the
                 pipelines. Such hydraulic restrictions may occur both with and without phase changes,
                 merely due to accumulation of a gas or a liquid in a pipe due to variations in geometry or
                 due to evaporation or condensation. Such examples may include water or liquid holdup in
                 a low spot creating resistance to flow, a viscous emulsion accumulation in a process vessel
                 reducing its effective volume or a vapor lock at the intake of a centrifugal pump breaking
                 fluid continuity. Each may restrict or interrupt flow. Additional cases of restrictions pertain
                 to fluids flowing outside their normal operating conditions. Such examples include pro-
                 duction chemicals slack flow which may cause a blockage in a chemical delivery umbilical
                 tube. Slack flow is a generalization term which means the fluid flows at a pressure below
                 its vapor pressure or bubble point. This may occur in late life production in deep water
                   operations when produced fluid has a lower density than the production chemical injected
                 at the subsea tree, and the flowing wellhead pressure is lower than the hydrostatic pressure
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