*******************************************
                *               AGI Profile               *
                * ACID GAS INJECTION PRESSURE CALCULATION *
                *               Version 1.4               *
                *             Copyright 1997              *
                *      Gas Liquids Engineering Ltd.       *
                *       #300, 2749 - 39 Avenue NE         *
                *   Calgary, Alberta  CANADA   T1Y 4T8    *
                * J.J. Carroll                  May  1999 *
                *******************************************


      RUN DATE: Aug. 30, 1999
      ---------
 
      PROJECT: CO2 Sequestration                       
      -------- 

      WELL PROFILE:
      -------------

              Depth      Pressure    Temperature      Density
               (m)        (kPa)        (deg C)       (kg/m**3)
              ------    ----------   -----------    -----------
               250.0    2.6760E+03    5.0000E+00    6.4033E+01
               237.5    2.6682E+03    5.2500E+00    6.3853E+01
               225.0    2.6604E+03    5.5000E+00    6.3498E+01
               212.5    2.6526E+03    5.7500E+00    6.3146E+01
               200.0    2.6449E+03    6.0000E+00    6.2798E+01
               187.5    2.6373E+03    6.2500E+00    6.2454E+01
               175.0    2.6297E+03    6.5000E+00    6.2114E+01
               162.5    2.6221E+03    6.7500E+00    6.1777E+01
               150.0    2.6146E+03    7.0000E+00    6.1443E+01
               137.5    2.6071E+03    7.2500E+00    6.1113E+01
               125.0    2.5996E+03    7.5000E+00    6.0787E+01
               112.5    2.5922E+03    7.7500E+00    6.0464E+01
               100.0    2.5848E+03    8.0000E+00    6.0144E+01
                87.5    2.5775E+03    8.2500E+00    5.9827E+01
                75.0    2.5702E+03    8.5000E+00    5.9514E+01
                62.5    2.5629E+03    8.7500E+00    5.9204E+01
                50.0    2.5557E+03    9.0000E+00    5.8896E+01
                37.5    2.5485E+03    9.2500E+00    5.8592E+01
                25.0    2.5414E+03    9.5000E+00    5.8291E+01
                12.5    2.5343E+03    9.7500E+00    5.7992E+01
                  .0    2.5272E+03    1.0000E+01    5.7697E+01

     Estimated injection pressure =  2.5272E+03 kPa

     Frictional pressure drop =  0.000E+00 kPa/m - input by user


     STREAM DIAGNOSTICS:
     -------------------

        DENSITY CORRELATION: Peng-Robinson equation of state - volume shifted
                             (SiPPS Version 2.0 -- (C) J.J. Carroll, 1993)

        SPECIFIED PHASE: gas - ** User should verify **

        MIXTURE MOLAR MASS:  44.010 kg/kmol

        ESTIMATED VISCOSITY:
             Bottom hole conditions: 1.534E-05 Pa.s
                                     1.534E-02 centipoise
             Surface conditions:     1.548E-05 Pa.s
                                     1.548E-02 centipoise
             Approximate average:    1.541E-05 Pa.s
                                     1.541E-02 centipoise

        DENSITY RANGE:
             Maximum Density: 6.403E+01 kg/m**3
             Minimum Density: 5.770E+01 kg/m**3
             Approx. Average: 6.086E+01 kg/m**3

        STREAM COMPOSITION       (mole %)   (wt %)
             CARBON DIOXIDE      100.000   100.000

     INTEGRATION DIAGNOSTICS:
     ------------------------

        Maximum integration error: 6.683E-08 kPa/m
        Number of integration steps:  20
        Initial step size: 1.250E+01 m
        Maximum step size: 1.250E+01 m
        Minimum step size: 1.250E+01 m
        Step size halved    0 times
        Step size doubled   0 times

        Integration completed without step-size modification