Page 210 - Handbook Of Multiphase Flow Assurance
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208                           7.  Flow assurance deliverability issues

                   Another cold flow design is static mixer. The static mixer design has been validated in
                 the field (Turner and Talley, 2008) to control the hydrate formation and to keep hydrates dis-
                 persed and flowing.
                   None of the cold flow methods have been implemented for continuous field use due to
                 novelty and lack of historic performance. Operators are not yet certain whether either cold
                 flow technique can deliver 100% reliability over the life of field. Cold flow technology may be
                 useful where the use of chemicals is restricted by local regulation.

                 Heavy oil viscosity

                   Heavy oils provide increased resistance to flow not only by being heavy but also by having
                 higher viscosity.
                   Over 20 methods are available in literature for estimating oil viscosity. These methods have been
                 summarized by Bergman and Sutton (2007) who correlated dead oil viscosity with temperature
                 and density based on 9837 viscosity measurements from 3047 fluids which ranged in API gravity
                 from 0.45° to 135.9°. The Bergman and Sutton correlation was discussed earlier in Chapter 3.
                   A recent correlation for estimating the viscosity of heavy oil in mixtures with water has
                 been presented by Wen et al. (2016). The method proposed by Wen may be used together with
                 the correlation provided by Bergman and Sutton (2007).


                 Emulsion rheology
                   Oil and water emulsion may be more viscous than just oil by a factor of 10 or more. Several
                 correlations for emulsion viscosity had been developed including Smith & Arnold, Woelflin
                 Loose, Woelflin Medium and Woelflin Tight.
                   Emulsions may exhibit peak viscosity around 50–85% water cut. The inversion point from
                 oil-external to water-external emulsion depends on the character of the crude, the character
                 of the brine, and the degree of emulsification. The inversion points corresponds to maximum
                 viscosity (Fig. 7.1).


                                                       Emulsion Viscosity
                            100,000


                           Effective  Emulsion Viscosity,  cP  10,000






                              1000
                                                                              Smith & Arnold
                                                                              Woelflin Loose
                                                                              Woelflin Medium
                                                                              Woelflin Tight
                               100
                                 0.0    0.1    0.2   0.3    0.4    0.5   0.6    0.7    0.8
                                                          Water Cut
                 FIG. 7.1  Effective emulsion viscosity correlations comparison.
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