Page 310 - Principles of Applied Reservoir Simulation 2E
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Part  V: Technical  Supplements  295


        Similar definitions of transmissibility apply in all three coordinate directions.


                      28.3 Terminology and General  Comments


             Some of the fluid property terms that are most frequently used in black
        oil simulation are defined here.


        Density
             Density is defined as the mass of a substance  divided by the volume it
        occupies.  The  density  of a  fluid  depends  on the  pressure,  temperature,  and
        composition of the fluid.


        Composition
             The composition of a fluid depends on whether the fluid consists of a pure
        component, such as water or methane, or is a mixture. For example, petroleum
        and  in situ water are mixtures. Petroleum is a mixture of hydrocarbon  com-
       pounds, and in situ water usually contains dissolved solids, such as salt, and may
        contain dissolved gases such as methane and carbon dioxide. The composition
        of a fluid is a list of the components contained in the fluid.
             The relative amount of each component in a mixture is defined  as the
        concentration  of the component.  Concentration  may be expressed in a variety
        of  units,  such  as  volume  fraction,  weight  fraction,  or  molar  fraction.  It  is
        important to know the units associated with the composition.  If the concentration
       units are not clearly expressed in a fluid report, they should be determined before
       use  in  calculations.  It  is  common  to  find  composition  expressed  in  mole
        fractions.  The symbols  {*„>>„ z t}  are often used to denote the mole fraction  of
        component i in the oil phase, gas phase, and wellstream respectively.
             The equilibrium K value is a measure of the amount of component i in
       the gas phase relative to the oil phase. It is defined  as the ratio
                                    K,  =  y./x t
       If component i exists entirely in the oil phase, then^, is 0 and K { is 0. Conversely,
                                                                approaches
       if component i exists entirely in the gas phase, then x t  is 0 and K f
       infinity.  Thus, the equilibrium K value for component  /  may  range from  0 to
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