Page 294 - Hydrocarbon Exploration and Production Second Edition
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Surface Facilities                                                    281


             11.1.3.1. Pressure reduction
             Gas is sometimes produced at very high pressures which have to be reduced for
             efficient processing and to reduce the weight and cost of the process facilities. The
             first pressure reduction is normally made across a choke before the well fluid enters
             the primary oil–gas separator.
                Note that primary separation has already been described in Section 11.1.2.




             11.1.3.2. Gas dehydration
             If produced gas contains water vapour, it may have to be dried (dehydrated). Water
             condensation in the process facilities can lead to hydrate formation and may cause
             corrosion (pipelines are particularly vulnerable) in the presence of carbon dioxide
             and hydrogen sulphide. Hydrates are formed by physical bonding between water
             and the lighter components in natural gas. They can plug pipes and process
             equipment. Charts such as the one given in Figure 11.14 are available to predict
             when hydrate formation may become a problem.
                Dehydration can be performed by a number of methods: cooling, absorption
             and adsorption. Water removal by cooling is simply a condensation process; at lower
             temperatures the gas can hold less water vapour. This method of dehydration is
             often used when gas has to be cooled to recover heavy hydrocarbons. Inhibitors such
             as glycol may have to be injected upstream of the chillers to prevent hydrate
             formation.
                One of the most common methods of dehydration is absorption of water vapour
             by tri-ethylene glycol (TEG) contacting. Gas is bubbled through a contact tower and
             water is absorbed by the glycol. Glycol can be regenerated by heating to boil off
             the water. In practice, glycol contacting will reduce water content sufficiently to
             prevent water dropout during evacuation by pipeline. Glycol absorption should not
             be confused with glycol (hydrate) inhibition, a process in which water is not
             removed (Figure 11.15).

                       1000




                     Pressure (bar)  100  Hydrate   No Hydrate



                        10



                         1
                           0               10               20               30
                                               Temperature (°C)
             Figure 11.14  Hydrate prediction plot.
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