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Modelling facility for field-average saturation 

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bodys(t) = \{ s_w(t), \, s_o(t), \, s_g(t) \}
 and  formation pressure 
LaTeX Math Inline
bodyp(t)
 at any time moment 
LaTeX Math Inline
bodyt
 as response to production flowrates history:


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anchorSw
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\frac{ds_w}{dt} =\frac{1}{A_e \, h_e \, \phi_e(p)} \left[ q^{\downarrow}_w(t) - q^{\uparrow}_w(t) + q^{\downarrow}_{WAQ}(t) \right] -  \left[ c_r(p) s_w +c_w(p) s_w  \right] \frac{dp}{dt}



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anchorSo
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\frac{ds_o}{dt} =\frac{1}{A_e \, h_e \, \phi_e(p)} \left[ q^{\downarrow}_o(t) - q^{\uparrow}_o(t) \right] -  \left[ c_r(p) s_o +c_o(p) s_o  \right] \frac{dp}{dt}



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\frac{ds_g}{dt} =\frac{1}{A_e \, h_e \, \phi_e(p)} \left[ q^{\downarrow}_g(t) - q^{\uparrow}_g(t) + q^{\downarrow}_{GC}(t) \right] -  \left[ c_r(p) s_w +c_g(p) s_g  \right] \frac{dp}{dt}



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anchors
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s_w + s_o + s_g = 1


where

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bodyp_i = p(0)

LaTeX Math Inline
body\Delta Q (t)

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bodyA_e

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bodyQ^{\uparrow}_t(t)

full-field cumulative offtakes by the time moment

LaTeX Math Inline
bodyt

LaTeX Math Inline
bodyh_e

LaTeX Math Inline
bodyQ^{\downarrow}_t(t)

full-field cumulative intakes by the time moment

LaTeX Math Inline
bodyt

LaTeX Math Inline
body\phi_e(p)

effective porosity as function of formation pressure 

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bodyp(t)
 

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bodyQ^{\downarrow}_{GC}(t)

cumulative volumetric inflow from Gas Cap Expansion

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bodyc_t(p)


total compressibility as function of formation pressure 

LaTeX Math Inline
bodyp(t)

LaTeX Math Inline
bodyQ^{\downarrow}_{AQ}(t)

cumulative volumetric inflow from Aquifer Expansion


The direct consequence of the above equations:

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anchorMatBal
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 A_e \, h_e \int_{p_i}^p \phi_e(p) \, c_t(p) \, dp  = \Delta Q (t) =  Q^{\downarrow}_t(t) - Q^{\uparrow}_t(t) + Q^{\downarrow}_{GC}(t) + Q^{\downarrow}_{AQ}(t)


The MatBal equation 

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anchorMatBal
  is often complemented by constant PI  model of Bottom-Hole Pressure (
LaTeX Math Inline
bodyp^{\uparrow}_{wf}(t)
 for producers and 
LaTeX Math Inline
bodyp^{\downarrow}_{wf}(t)
 for injectors):


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anchorBHP_PROD
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p^{\uparrow}_{wf, k}(t) = p(t) - {J^{\uparrow}_k}^{-1} \cdot \frac{dQ^{\uparrow}_k}{dt}



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anchorBHP_INJ
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p^{\downarrow}_{wf, \, j}(t) = p(t) -  {J^{\downarrow}_j}^{-1} \cdot \frac{dQ^{\downarrow}_j}{dt}


wherewhere

LaTeX Math Inline
bodyp^{\uparrow}_{wf, \, k}(t)

BHP in

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bodyk
-th producer

LaTeX Math Inline
bodyp^{\downarrow}_{wf, \, j}(t)

BHP in

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bodyj
-th injector

LaTeX Math Inline
bodyQ^{\uparrow}_k(t)

cumulative offtakes from

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bodyk
-th producer by the time moment
LaTeX Math Inline
bodyt

LaTeX Math Inline
bodyQ^{\downarrow}_j(t)

cumulative intakes to

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bodyj
-th injector by the time moment
LaTeX Math Inline
bodyt

LaTeX Math Inline
bodyJ^{\uparrow}_k

productivity index of

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bodyk
-th producer

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bodyJ^{\downarrow}_j

injectivity Index of

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bodyj
-th injector



In practice there is no way to measure the external influx 

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bodyq^{\downarrow}_{GC}(t)
 and 
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bodyq^{\downarrow}_{AQ}(t)
 so that one need to model them and calibrate model parameters to fit available data on production flowrates history and formation pressure data records. 

There is a list of various analytical Aquifer Drive and  Gas Cap Drive models which are normally related to pressure dynamics 

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bodyp(t)
:

Gas Cap Drive @model Aquifer Drive @model


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anchor1
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q^{\downarrow}_{GC}(t) = q^{\downarrow}_{GC}(p(t))



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anchor1
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q^{\downarrow}_{AQ}(t) = q^{\downarrow}_{AQ}(p(t))


which closes a set of equations 

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anchorSw
LaTeX Math Block Reference
anchors
 for the pressure 
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bodyp(t)
 and saturations 
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body\{ s_w, \, s_o, \, s_g \}
.


Variations



In some specific cases equation 

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anchorMatBal
can be explicitly integrated:

Low pressure dry gas

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body\{ \phi_e = {\rm const}, \ c_t = {\rm const} \}

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bodyc_t = c_r + \frac{1}{p} \sim \frac{1}{p}


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anchorQ6XP7
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p(t)  = p_i + \frac{\Delta Q(t)}{V_e \cdot c_t}



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p(t)  = p_i \exp \left[ \frac{\Delta Q(t)}{V_e \cdot c_t} \right]


where

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bodyV_e = A_e \, h_e \, \phi_e

drainage volume




See Also


Petroleum Industry / Upstream /  Production / Subsurface Production / Field Study & Modelling / Production Analysis

Material Balance Analysis (0D or MatBal)