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The One of the Productivity Diagnostics methods  based on relation between the bottom-hole pressure 

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bodyp_{wf}
 and surface flow rate  
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bodyq
  during the stabilised formation flow (see the reference to original paper of Gilbert):

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p_{wf} = p_{wf}(q)

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Fig. 1

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One of the two key concepts of Well Flow Performance analysis along with Vertical Lift Performance (VLP).

The word  "Inflow" is misnomer as Inflow Performance Relationship (IPR) analysis is applicable for both producers and injectors.


The most general proxy-model is given by LIT (Laminar Inertial Turbulent) IPR model:

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a \, q + b \, q^2 = \Psi(p_r) - \Psi(p_{wf})

where

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bodyp_r

static wellbore pressure

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bodya

laminar flow coefficient

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bodyb

turbulent flow coefficient

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body\Psi(p)

pseudo-pressure function specific to fluid type


It needs well tests at least three different rates to assess  

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body--uriencoded--\%7B a \, , \, b, \, p_r \%7D
 but obviously more tests will make assessment more accurate.


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The Inflow Performance Relationship (IPR) analysis is closely related to well Productivity Index (PI)  

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bodyJ_s
 which is defined as below:

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The  Productivity Index can be constant (showing a straight line on IPR like on  Fig. 12) or dependent on bottomhole pressure 

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bodyp_{wf}
  or equivalently on flowrate 
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bodyq
 (showing a curved line on IPR like on  Fig. 23) .

In general case of multiphase flow the PI 

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

For undersaturated reservoir the numerically-simulated Inflow Performance Relationship (IPR)s have been approximated by analytical models and some of them are brought below. 

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These correaltions should be calibrated to the available well test data to set a up a customised IPR model for a given formation.


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Fig1
Fig1

Water and Dead Oil IPR

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

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bodyJ_s = \rm const
 and IPR plot is reperented represented by a straight line (Fig. 12)


Fig. 12. IPR plot for constant productivity (water and dead oil)

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This is a typical IPR plot for water supply wells, water injectors and dead oil producers.

The For the oil/water production the PI can be estimated using the Darcy equation Dupuit PI @model:

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J_s = \frac{2 \pi \sigma}{ \ln \frac{r_e}{r_w} + \epsilon+ S}

where 

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body\sigma = \Big \langle \frac{k} {\mu} \Big \rangle \, h = k \, h\, \Big[ \frac{k_{rw}}{\mu_w} + \frac{k_{ro}}{\mu_o} \Big]
 – water-based or water-oil-based transmissbility transmissibility above bubble point 
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pageLinear Perrine multi-phase diffusion @model
,

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The alternative form of the constant Productivity Index  IPR is given by:

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\frac{q}{q_{max}} = 1 -\frac{p_{wf}}{p_r}

where 

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bodyq_{max} = J_s \, p_R
  is the maximum reservoir deliverability when the bottom-hole is at atmospheric pressure and also called Absolute Open Flow (AOF).


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Fig2
Fig2

Dry Gas IPR

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For gas producers, the fluid compressibility is high and formation flow is essentially non-linear, inflicting the downward trend on the whole IPR plot (Fig. 23).


Fig. 23. IPR for dry gas producer or gas injector into a gas formation

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where 

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bodyn
 is the turbulent flow exponent, equal to 0.5 for fully turbulent flow and equal to 1 for laminar flow.

The more accurate approximation is given by LIT (Laminar Inertial Turbulent) IPR model:

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a \, q + b \, q^2 = \Psi(p_r) - \Psi(p_{wf})

where 

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body\Psi
 – is pseudo-pressure function specific to a certain gas PVT model,  
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bodya
 is laminar flow coefficient and 
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 is turbulent flow coefficient.It needs two well tests at two different rates to assess 
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body\{ q_{max} \, , \, n \}
 or 
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body\{ a \, , \, b \}
.  

But obviously more tests will make assessment more accruate.


Saturated Oil IPR

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For saturated oil reservoir the free gas flow inflict the downward trend of IPR plot  similar to dry gas (Fig. 34).


Fig. 34. IPR for 2-phase oil+gas production below and above bubble point

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Vogel IPR @ model
Vogel IPR @ model
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Undersaturated Oil IPR

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For undersaturated oil reservoir 

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bodyp_r > p_b
 the behavior of IPR model will vary on whether the bottom-hole pressure is above or below bubble point.

When it is higher than bubble point 

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bodyp_{wf} > p_b
 then formation flow will be single-phase oil and production will follow the constant Inflow Performance Relationship (IPR)

When bottom-hole pressure goes below bubble point 

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bodyp_{wf} < p_b
  the near-reservoir zone free gas slippage also inflicts the downward trend at the right side of IPR plot (Fig. 35).

It can be interpreted as deterioration of near-reservoir zone permeability when the fluid velocity is high and approximated by rate-dependant skin-factor.


Fig. 35. IPR for 2-phase oil+gas production below and above bubble point

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q_{max} = q_b \, \Big[1 + \frac{1}{1.8} \frac{p_b}{(p_r - p_b)}  \Big]




Saturated Multiphase IPR

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For saturated 3-phase water-oil-gas reservoir the IPR analysis is represented by oil and water components separately (see Fig. 46.1 and Fig. 46.2).


Fig. 46.1. Oil IPR for saturated 3-phase (water + oil + gas) formation flow

Fig. 46.2. Water IPR for saturated 3-phase (water + oil + gas) formation flow

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\frac{q_w}{q_{w, \, max}} = 1 - 0.72 \, \frac{p_{wf}}{p_r} - 0.28 \Bigg(\frac{p_{wf}}{p_r} \Bigg)^2 

Undersaturated Multiphase IPR

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For undersaturated 3-phase water-oil-gas reservoir the IPR analysis is represented by oil and water components separately (see Fig. 47.1 and Fig. 47.2).


Fig. 47.1. Oil IPR for udersaturated 3-phase (water + oil + gas) formation flow

Fig. 47.2. Water IPR for undersaturated 3-phase (water + oil + gas) formation flow

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The analytical correlation for saturated 3-phase oil flow is given by Wiggins model:

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\frac{q_o}{q_{o, \, max}} = 1 - 0.52 \, \frac{p_{wf}}{p_r} - 0.48 \Bigg(\frac{p_{wf}}{p_r} \Bigg)^2  
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\frac{q_w}{q_{w, \, max}} = 1 - 0.72 \, \frac{p_{wf}}{p_r} - 0.28 \Bigg(\frac{p_{wf}}{p_r} \Bigg)^2 

See Also

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Petroleum Industry / Upstream /   Production / Subsurface Production / Well & Reservoir ManagementSubsurface E&P Disciplines / Field Study & Modelling / Production Analysis / Productivity Diagnostics

Production Technology / Well Flow Performance ]

Vogel IPR @model ] [ Richardson and Shaw IPR @ model ] Wiggins IPR @ model ][ LIT IPR @ model ][ PADE IPR @ model ]

Dual-layer IPR][ Multi-layer IPR ] [ Dual-layer IPR with dynamic fracture ]


Reference

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Gilbert
Gilbert
Gilbert, W.E.: "Flowing and Gas-Lift Well Performance," Drill. and Prod. Prac., API (1954) 126.

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