MATERIAL BALANCE EQUATION - I

Performance Prediction For Solution_Gas-Gas_Cap Drive Reservoir


INPUT   DATA EXAMPLE Of Input/Output

Title  

  PVT    DATA     
  Pressure   Oil FVF
Bo  
Solution GOR
Rs  
Gas FVF
Bg  
Oil Viscosity
μo  
Gas Viscosity
μg  
  #    psi    rbbl/stb   scf/stb   rbbl/scf    cp     cp  
1 max.
2
3
4
5
6
7
8
9
10
11
12
13
14
15

  RELATIVE  PERMEABILITY   DATA     
  Total
Liquid
Saturation
SL  
Relative
Permeability
Ratio
(kg/ko)  
  #     
1 min.
2
3
4
5
6
7
8
9
10
11
12
13
14
15

  RESERVOIR  &   WELL   DATA     
Initial Water Saturation fraction
Original Oil In Place bbls
Gas Cap to Oil Pore Vol ratio 
Number of Wells  
Average Initial PI of wells bbl/psi
Well FBH pressure psi


     Reset


OUTPUT   VARIABLES   &   GRAPHS


 PressureCumulative
Oil Production
Instantaneous
Gas Oil Ratio
Cumulative
Gas Production
Krg/kro Oil Recovery
Factor
Oil Production
Rate
Time
#psibblscf/bblscf  bbl/daymonths 
1
2
3
:

THEORY  &   FORMULAE

Material Balance Equation - Solution Gas Drive/Gas-Cap Drive

The M.B.E. remains an important analytical tool in reservoir engineering, employed mainly in the preliminary design of reservoir development and operations, prelude/complement to fully-fledged reservoir simulation, and in economic/planning studies.

The modified Schilthuis procedure is implemented here to compute oil and gas production from a combination of solution gas drive/gas-cap drive reservoir producing at or below the bubble-point pressure. Direct production/injection of gas fro/to the gas cap is not included here. It is assumed that the gas-oil contact does not move into the oil zone, but gas expansion from the gas cap will diffuse through the oil zone. Also water encroachment is considered negligible.

User Input: The user is expected to enter PVT and Relative-Permeability data, each consisting of 10 to 15 data points. The PVT pressure values should be in descending order and pressure intervals must be constant. The liquid saturation values in the Rel. Perm table, should be in ascending order rising to 1.0. For rate-time prediction, the required data are: number of oil wells, and the wells' average initial productivity index and flowing bottomhole pressure. Not all the wells are considered active in day one. A constant drilling policy is assumed, i.e. a more or less equal number of new wells are brought into production at each new pressure step.

The main MBE equation and three auxillary equations are given below:

    

where:
     SDI = solution gas drive index
     GDI = gas-cap gas drive index
     N = initial oil in place, bbl
     NPn = cumulative oil produced at pressure step n, fraction of N
     GPn = cumulative gas produced at pressure step n, fraction of N
     Mi = initial ratio of gas-cap to oil reservoir pore space
     Bt = two-phase formation vol. factor at pressure step n
     Bo = oil formation vol. factor at pressure step n
     Boi = initial oil formation volume factor, bbl/scf
     Bgn = gas formation vol. factor at pressure step n
     Bgi = initial gas formation volume factor, res.bbl/scf
     Rsn = solution gas-oil ratio at pressure step n
     Rsi = initial solution gas-oil ratio, scf/bbl
     RIn = instataneous gas-oil ratio
     SLn = total liquid saturation at pressure step n
     Sw = water saturation
     μ = viscosity, cp
     k = permeability, mD

The productivity index (J) decline relative to the initial productivity index (Ji) is approximated by:
          J = Ji[1 - Swi]3oBo]/ [μoiBoi]

The cubic spline interpolation method is used to generate continuous values of relative perm. data from the entered set of discrete values.

BIBLIOGRAPHY