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LaTeX Math Inline
bodyp_R

field-average formation pressure within the drainage area

LaTeX Math Inline
bodyV_e
of a given well:
LaTeX Math Inline
bodyp_R = \frac{1}{V_e} \, \int_{V_e} \, p(t, {\bf r}) \, dV


Water and Dead Oil IPR

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Based on these notions above defintions the general WFP – Well Flow Performance can be wirtten in universal a general form:

LaTeX Math Block
anchorIPR
alignmentleft
p_{wf} = p_R - \frac{q}{J_s}

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LaTeX Math Inline
body-

for producer

LaTeX Math Inline
body+

for injector

LaTeX Math Inline
bodyq=q_{\rm liq}=q_o+q_w

for oil producer

LaTeX Math Inline
bodyq=q_g

for gas producer or injector

LaTeX Math Inline
bodyq=q_w

for water injector or water-supply producer


The  Productivity Index can be constant or dependent on bottom-hole pressure

LaTeX Math Inline
bodyp_{wf}
.



For a single layer formation with low-compressibility fluid (like water or dead oil) the PI does not depend on drawdown (or flowrate) 

LaTeX Math Inline
bodyJ_s = \rm const
 and WFP – Well Flow Performance plot is reperented by a straight line (Fig. 1)

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Fig.1. WFP – Well Flow Performance plot for constant productivity (water and undersaturated dead oil)


This is a typical WFP – Well Flow Performance plot for water supply wells, water injectors and dead oil producers above bubble point.


The PI can be estimated using the Darcy equation:

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LaTeX Math Inline
body\epsilon = 0.5
 for steady-state SS flow and 
LaTeX Math Inline
body\epsilon = 0.75
 for pseudo-steady state PSS flow.


Dry Gas IPR

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For gas producers, the fluid compressibility is high and formation flow in well vicinity becomes non-linear (deviating from Darcy) fot high flowrates, inflicting the downward trend on WFP – Well Flow Performance plot (Fig. 2).

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Fig. 2. WFP – Well Flow Performance for gas reservoirdry gas producer or gas injector into a gas formation



In general case of saturated oil, the PI 

LaTeX Math Inline
bodyJ_s
 features a complex dependance on bottom-hole pressure 
LaTeX Math Inline
bodyp_{wf}
( or flowrate 
LaTeX Math Inline
bodyq
) which can be etstablished based on numerical simulations of multiphase formation flow.

But when field-average formation pressure is above bubble-point 

LaTeX Math Inline
bodyp_R > p_b
 (which means that most parts of the drainage area are saturated oil) the PI can be farily approximated  by some analytical correlations.



Saturated Oil IPR

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For 2-phase oil-gas formation flow below bubble point 

LaTeX Math Inline
bodyP_{wf} < P_b
  the free gas slippage effects inflict the downward trend on WFP – Well Flow Performance plot (Fig. 3).

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Fig. 3. WFP – Well Flow Performance for 2-phase oil+gas production below and above bubble point


Multiphase IPR

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For 3-phase water-oil-gas flow the IPR analysis is perfomed on oil and watr components (see Fig. 4.1 and Fig. 4.2).

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