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Hydrate of natural gas                      129

            Cold flow
              Cold flow had been proposed as a way to achieve chemical-free production in subsea sys-
            tems. The concept involves forming a suspension of hydrate particles and recirculation of
            a fraction of the stream with hydrate particles into the uninhibited produced fluid stream.
            Hydrate particles from the recycle stream will act as nucleation sites for the conversion of
            water in the main stream to hydrate. Hydrate will grow on the suspended particles without
            adhesion to pipe walls. The recycle stream needs to be added at a position in a flowline where
            produced fluid stream has cooled down to the hydrate formation condition. The cold flow
            method had been evaluated in laboratory setting in 2003 and showed good results for both
            hydrate control and promising results for wax deposit control. The results were published
            (US7261810 patent, 2003; Wolden et al., 2005). However, economics of the cold flow approach
            are constrained by the need for a recirculation pump located close to the wellhead, a recycle
            stream pipeline and the increased viscosity of the hydrate suspension. The combination of
            these requirements makes cold flow applicable only in a narrow range of flowline distances.
            This method has not been tested in the field. Another implementation of cold flow with a field
            pilot test was reported by Turner and Talley (2008).
            Partial gas separation
              Partial gas separation may be used to avoid hydrate if supported by appropriate labo-
            ratory verification. With low GOR oils, the amount of gas available to form hydrate is low.
            Partial gas separation may remove enough gas from the hydrocarbon mixture to shift hydrate
            equilibrium outside the operating envelope. The method can be modeled with PVT software
            but the true shift of hydrate stability conditions should be validated in a laboratory.
            Static mixer
              Static mixer concept for hydrate control has been tested in the field with promising re-
            sults. The summary of the method and the field test had been presented at the 2008 ICGH in
            Edmonton, Canada (ICGH, 2008).

            Modeling of gas hydrates
              Currently several rigorous models are available for calculation of gas hydrate stability.
            These models have been developed based on the van der Waals and Platteau 1959 work
            which has been discussed in Sloan (1990).
              Early  practical  examples  of software  implementation  for modeling  of  hydrate  stability
            were developed by Robinson (1988) and Erickson (1983) with the source code presented in
            the dissertation.
              The working version  of  the software for use  on PC computers  is also available  at  the
            Colorado School of Mines, as described in Chapter 11. This software should be able to help
            achieve safe operation of production facilities and to raise awareness of operators about gas
            hydrates.
              A number of empirical correlations have been presented over the years.
              Katz had developed a graphical method to find hydrate formation conditions for natural
            gases with various gravities (Katz, 1945; Katz et al., 1959). A detailed example of this method
            allowing one to calculate the gas gravity and to find the appropriate hydrate conditions is
            also presented in Sloan (1990).
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