Difference between revisions of "3 Phase IPR"

From wiki.pengtools.com
Jump to: navigation, search
(→‎3 Phase IPR calculation example)
 
(62 intermediate revisions by the same user not shown)
Line 1: Line 1:
 
__TOC__
 
__TOC__
 
==Three-phase Inflow Performance Relationship==
 
==Three-phase Inflow Performance Relationship==
−
[[File:3 Phase IPR Curve.png|thumb|right|300px|3 Phase IPR Curve <ref name=KermitBrown1984/>]]
+
[[File:3 Phase IPR Curve.png|thumb|right|400px|3 Phase IPR Curve <ref name=KermitBrown1984/>]]
  
−
[[3 Phase IPR]] calculates IPR curve for oil wells producing water.
+
[[3 Phase IPR]] is an [[IPR]] curve calculated on the basis of total barrels of produced fluid, including gas.
  
−
[[3 Phase IPR]] equation was derived by Petrobras based on combination of [[Vogel's IPR]] equation for oil flow and constant productivity for water flow <ref name=KermitBrown1984/>.
+
[[3 Phase IPR]] curve is used in [[:Category:PumpDesign|Pump Design]] software for pump sizing.
−
 
 
−
[[3 Phase IPR]] curve is determined geometrically from those equations considering the fractional flow of oil and water  <ref name=KermitBrown1984/>.
 
  
 
==Math and Physics==
 
==Math and Physics==
−
Total flow rate equations:
+
The volume of 1 stb of liquid plus associated gas at any pressure and temperature is given by<ref name=KermitBrown1984/>:
−
 
+
:<math> VF=WCUT\ B_w + (1-WCUT)\ B_o + (GLR\ - (1-WCUT)R_s - WCUT\ R_{sw})B_g</math> <ref name=KermitBrown1984/>
−
===For P<sub>b</sub> < P<sub>wf</sub> < P<sub>r</sub>===
 
−
For pressures between reservoir pressure and bubble point pressure:
 
−
:<math> q_t =J (P_r - P_{wf})</math> <ref name=KermitBrown1984/>
 
−
 
 
−
===For P<sub>wfG</sub> < P<sub>wf</sub> < P<sub>b</sub>===
 
−
For pressures between the bubble point pressure and the flowing bottom-hole pressures:
 
−
:<math> q_t =\frac{-C+\sqrt{C^2-4B^2D}}{2B^2}\ for B \ne 0</math><ref name=KermitBrown1984/>
 
−
:<math> q_t =D/C\ for B = 0</math><ref name=KermitBrown1984/>
 
  
−
where:
 
  
−
:<math> A=\frac{P_{wf}+0.125F_oP_b-F_wP_r}{0.125F_oP_b}</math><ref name=KermitBrown1984/>
+
The total volume of produced fluid rate (liquid plus gas) at any conditions of pressure and temperature:
−
:<math> B=\frac{F_w}{0.125F_oP_bJ}</math><ref name=KermitBrown1984/>
+
:<math> V=q_{t_{sc}} \times VF</math> <ref name=KermitBrown1984/>
−
:<math> C=2AB+\frac{80}{q_{o_{max}}-q_b}</math><ref name=KermitBrown1984/>
 
−
:<math> D=A^2-80\frac{q_b}{q_{o_{max}}-q_b}-81</math><ref name=KermitBrown1984/>
 
  
−
=== For 0 < P<sub>wf</sub> < P<sub>wfG</sub>===
+
<math> q_{t_{sc}} </math> is calculated as usual using:
−
:<math> q_t =\frac{P_{wfG}+q_{o_{max}}tan(\beta)-P_{wf}}{tan(\beta)}</math><ref name=KermitBrown1984/>
+
:*[[Vogel's IPR]] equation
 +
:*[[Composite IPR]] equation
  
−
where:
+
==[[3 Phase IPR]] calculation example==
 +
Following the well #1 example given by Brown<ref name=KermitBrown1984 />on Figure 5.8, page 191:
  
−
:<math> tan(\beta) = CD/CG </math><ref name=KermitBrown1984/>
+
''In progress ...''
−
:<math> CD = F_w\frac{0.001q_{o_{max}}}{J}+F_o0.125P_b \left ( -1+\sqrt{81-80 \frac{0.999q_{o_{max}}-q_b}{q_{o_{max}}-q_b}} \right)</math><ref name=KermitBrown1984/>
 
−
:<math> CG = 0.001 q_{o_{max}}</math><ref name=KermitBrown1984/>
 
−
 
 
−
===And===
 
−
:<math> P_{wfG}=F_w \left ( P_r - \frac{q_{o_{max}}}{J}\right )</math><ref name=KermitBrown1984/>
 
−
:<math> q_{o_{max}}=q_b+\frac{JP_b}{1.8}</math><ref name=KermitBrown1984/>
 
−
 
 
−
==IPR calculator software==
 
−
*[[:Category:PQplot | PQplot]] nodal analysis software is used to calculate the [[IPR]] curves. [[:Category:PQplot | PQplot]]  is available online at [https://www.pengtools.com www.pengtools.com].
 
−
*Excel
 
−
*other
 
  
 
== Nomenclature  ==
 
== Nomenclature  ==
−
:<math> B </math> = formation volume factor, bbl/stb
+
:<math> B</math> = volume factor, bbl/stb oil; bbl/scf gas
−
:<math> J_D </math> = dimensionless productivity index, dimensionless
+
:<math> GLR</math> = gas liquid ratio, scf / bbl
−
:<math> kh</math> = permeability times thickness, md*ft
+
:<math> q </math> = flowing rate, stb/d
−
:<math> \bar{P} </math> = average reservoir pressure, psia
+
:<math> R</math> = solution gas ration, scf / stb
−
:<math> P_{\bar{P}} </math> = average reservoir pseudopressure, psia<sup>2</sup>/cP
+
:<math> V </math> = total volume of produced fluid rate (inducing gas), bbl/d
−
:<math> P_{wf} </math> = well flowing pressure, psia
+
:<math> VF </math> = volume factor, bbl/stb
−
:<math> P_{P_{wf}} </math> = average well flowing pseudopressure, psia<sup>2</sup>/cP
+
:<math> WCUT</math> = water cut, fraction
−
:<math> q </math> = flowing rate, stb/d
+
===Subscripts===
−
:<math> q_g </math> = gas rate, MMscfd
+
:g = gas<BR/>
−
:<math> T </math> = temperature, °R
+
:o = oil<BR/>
−
 
+
:sc = standard conditions<BR/>
−
===Greek symbols===
+
:t = total<BR/>
−
 
+
:w = water<BR/>
−
:<math> \mu </math> = viscosity, cp
 
  
−
=== References ===
+
== References ==
 
<references>
 
<references>
 
<ref name= KermitBrown1984 >{{cite book
 
<ref name= KermitBrown1984 >{{cite book
Line 75: Line 52:
  
 
==See also==
 
==See also==
−
:[[141.2 derivation]]<BR/>
+
:[[IPR]]<BR/>
 +
:[[Vogel's IPR]]<BR/>
 +
:[[Composite IPR]]<BR/>
 
:[[Darcy's law]]<BR/>
 
:[[Darcy's law]]<BR/>
−
:[[JD]]<BR/>
 
−
:[[Production Potential]]
 
  
 
{{#seo:
 
{{#seo:
Line 84: Line 61:
 
|titlemode= replace
 
|titlemode= replace
 
|keywords=Inflow Performance Relationship, nodal analysis, IPR curve, IPR calculator
 
|keywords=Inflow Performance Relationship, nodal analysis, IPR curve, IPR calculator
−
|description=Three-phase inflow performance relationship for oil wells producing water.
+
|description=Three-phase inflow performance relationship for total volume of produced rate (including free gas).
 
}}
 
}}
  
 
[[Category:PQplot]]
 
[[Category:PQplot]]
 +
[[Category:PumpDesing]]

Latest revision as of 07:51, 17 April 2019

Three-phase Inflow Performance Relationship

3 Phase IPR Curve [1]

3 Phase IPR is an IPR curve calculated on the basis of total barrels of produced fluid, including gas.

3 Phase IPR curve is used in Pump Design software for pump sizing.

Math and Physics

The volume of 1 stb of liquid plus associated gas at any pressure and temperature is given by[1]:

VF=WCUT\ B_w + (1-WCUT)\ B_o + (GLR\ - (1-WCUT)R_s - WCUT\ R_{sw})B_g [1]


The total volume of produced fluid rate (liquid plus gas) at any conditions of pressure and temperature:

V=q_{t_{sc}} \times VF [1]

q_{t_{sc}} is calculated as usual using:

3 Phase IPR calculation example

Following the well #1 example given by Brown[1]on Figure 5.8, page 191:

In progress ...

Nomenclature

B = volume factor, bbl/stb oil; bbl/scf gas
GLR = gas liquid ratio, scf / bbl
q = flowing rate, stb/d
R = solution gas ration, scf / stb
V = total volume of produced fluid rate (inducing gas), bbl/d
VF = volume factor, bbl/stb
WCUT = water cut, fraction

Subscripts

g = gas
o = oil
sc = standard conditions
t = total
w = water

References

  1. ↑ 1.0 1.1 1.2 1.3 1.4 Brown, Kermit (1984). The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis. Tulsa, Oklahoma: PennWellBookss. 

See also

IPR
Vogel's IPR
Composite IPR
Darcy's law
Retrieved from "https://wiki.pengtools.com/index.php?title=3_Phase_IPR&oldid=6158"