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Consider a system of net hydrocarbon pay and finite or infinite volume Aquifer as a radial composite reservoir with inner composite area being a Net Pay Area and outer composite area an Aquifer

(see schematic and notations on Fig. 1 at Radial VEH Aquifer Drive @model).

The Aquifer's outer boundary may be "no-flow" for finite-volume Aquifer or constant pressure for infinite-volume Aquifer.

The transient pressure diffusion in the outer (Aquifer) composite area is going to honour the following equation:

Driving equationInitial condition

Homogeneous Aquifer reservoir with

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body\chi(r)= \rm const

Initial Aquifer pressure is considered to be the same as Net Pay Area
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anchorRC
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\frac{\partial p_a}{\partial t} = \chi \cdot \left[ \frac{\partial^2 p_a}{\partial r^2} + \frac{1}{r}\cdot \frac{\partial p_a}{\partial r} \right]
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p_a(t = 0, r)= p(0)



Inner Aquifer boundaryOuter Aquifer boundary is one of the two below:
Pressure variation at the contact with Net Pay Are"No-flow" "Constant pressure" 
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p_a(t, r=r_e) = p(t)
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p1
p_PSS
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\frac{\partial p_a}{\partial r} 
\bigg|_{(t, r=r_a)} = 0
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anchorpconst
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 p_a(t, r = \infty) = 0


Consider dimensionless solution 

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bodyp_1(t_D, r_D)
of the following equation:

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\frac{\partial p_1}{\partial t_D} =  \frac{\partial^2 p_1}{\partial r_D^2} + \frac{1}{r_D}\cdot \frac{\partial p_1}{\partial r_D}
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p_1(t_D = 0, r_D)= 0



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p_1(t_D, r_D=1) = 1
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\frac{\partial p_1(t_D, r_D)}{\partial r_D} 
\Bigg|_{r_D=r_{aD}} = 0

or

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 \quad {\rm or} \quad  p_1(t_D, r_D = \infty) = 0

which represents a specific unique function of dimensionless time

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bodyt_D
and distance
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bodyr_D
.

...

One can easily check that

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anchorVEHP
honours the whole set of equations
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anchorRC
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anchorp1p_PSS
/
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anchorpconst
and as such defines a unique solution of the above problem.

Now having the pressure dynamics in hand one can calculate the water influx.

Water The water flowrate within

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body\theta
sector angle at the interface with oil reservoir will be net pay is:

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q^{\downarrow}_{AQ}(t)= \theta \cdot r_e \cdot h \cdot u(t,r_e)

where

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bodyu(t,r_e)
is flow velocity at aquifer Net Pay ↔ Aquifer contact boundary, which is:

...

where

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body--uriencoded--\displaystyle M = \frac%7Bk_w%7D%7B\mu_w%7D
is aquifer Aquifer mobility.


Water flowrate becomesThe water flowrate is going to be:

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q^{\downarrow}_{AQ}(t)= \theta \cdot r_e \cdot h \cdot M \cdot  \frac{\partial p_a(t,r)}{\partial r} \bigg|_{r=r_e}

Cumulative and cumulative water flux is going to be:

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Q^{\downarrow}_{AQ}(t) = \int_0^t q^{\downarrow}_{AQ}(t) dt = \theta \cdot r_e \cdot h \cdot M  \cdot \int_0^t \frac{\partial p_a(t,r)}{\partial r} \bigg|_{r=r_e} dt

...

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\xi = \tau + \frac{r_e^2}{\chi} \cdot t_D \rightarrow t_D = \frac{(\xi-\tau)\chi}{r_e^2} \rightarrow d\xi = \frac{r_e^2}{\chi} \cdot dt_D

and flux cumulative influx becomes:

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Q^{\downarrow}_{AQ}(t) = \theta  \cdot h \cdot M \cdot \frac{r_e^2}{\chi} \cdot \int_0^t \dot p(\tau) d\tau \int_0^{(t-\tau)\chi/r_e^2}  

\frac{\partial p_1( t_D, r_D)}{\partial r_D}  \Bigg|_{r_D=1} dt_D = B \cdot \int_0^t \dot p(\tau) d\tau \int_0^{(t-\tau)\chi/r_e^2}  

\frac{\partial p_1( t_D, r_D)}{\partial r_D}  \Bigg|_{r_D=1} dt_D

where

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bodyB
is water influx constant and which leads to:

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...

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Q^{\downarrow}_{AQ}= B \cdot \int_0^t W_{eD} \left( \frac{(t-\tau)\chi}{r_e^2}\right) \dot p(\tau) d\tau

where

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W_{eD}(t) = \int_0^{t} \frac{\partial p_1}{\partial r_D} \bigg|_{r_D = 1} dt_D 

is a unique dimensionless function of dimensionless time

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bodyt_D
which can be tabulated via numerical solution or approximated by closed-form expression and
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anchorWeD
.


See Also

...

Petroleum Industry / Upstream / Subsurface E&P Disciplines / Field Study & Modelling / Aquifer Drive / Aquifer Drive Models / Radial VEH Aquifer Drive @model

...