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CFD plays a key role


            in the optimization of finger type



            slug catchers





            A slug catcher is quite a complex piece of equipment, usually
            sized using simplified procedures. The drawback of this method
            is the need for conservative assumptions which hinder the
            achievement of a competitive design. CFD simulation provides a
            completely new design approach that can lead to significative
            savings in terms of investment cost and equipment footprint


            Francesco La Motta, Process Leader, Oil&Gas and Biogas Projects,
            Alessandro Boffa, Senior Process Engineer,
            OILTECH srl



            A

                         routine problem is the presence of
                         liquids  in  pipelines  that  transfer
                         untreated gas from gas fields to
                         processing plants. In this case,
                         the liquid arrival rate is irregular
                         rather than constant. Intermittent
            flows can reach much higher peaks than average
            flows. Obviously, the downstream liquid processing
            facilities cannot be sized for these peak conditions
            and a liquid separator is required to separate
            these “liquid slugs”, accumulating them and
            slowly releasing them to the downstream gas
            processing plants. Slug catchers solve this
            problem by acting as a buffer for the liquid
            flowrate and providing a temporary storage for the   gas flow. For example, during the “ramp-up”
            volume of liquid when peak flow is reached.  phase at the pipeline start up, the higher gas
            The draining rate of a slug catcher is set to empty   velocity can contribute to part of the liquid
            the equipment in time before the next liquid peak   accumulated inside the pipeline being carried
            (or “slug”) arrives.                         over.
            In  a  pipeline  transporting  natural  gas  and   •   The pigging operation displacing all the liquid
            associated liquids (light condensates and/or   from the pipeline into the slug catcher in a
            water), the amount of liquid found at the pipeline   relatively short time.
            outlet is determined by the following three factors:
            •   The  continuous  liquid  production  under   Normally, pigging gives the maximum slug volume
                steady flow conditions, depending on the   that must be taken into account for slug catcher
                gas-liquid  equilibrium  governed  by  sizing. The liquid volume accumulated in the
                composition and operating conditions.   pipeline and displaced during pigging mainly
            •   The intermittent or transient liquid production   depends on:
                due to variation of liquid inventory inside the   •   Composition
                pipeline caused by a significant increase in   •   Operating pressure and temperature

                                                                               IndustrIal Plants - September 2021
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