Fracture Geometry Models - PKN, KGD, and Radial

Overview

Classical 2D fracture models predict the geometry of a hydraulically induced fracture -- its width, length (or radius), net pressure, and volume -- as functions of injection rate, fluid properties, rock properties, and time. Three fundamental models serve as the foundation for fracture design:

Model Full Name Year Key Assumption
PKN Perkins-Kern-Nordgren 1961/1972 Vertical plane strain, confined height
KGD Khristianovic-Geertsma-de Klerk 1955/1969 Horizontal plane strain, confined height
Radial Penny-shaped (Sneddon) 1946 No height confinement, radial symmetry

All three models solve the coupled problem of:

  1. Elasticity -- rock deformation under internal fluid pressure
  2. Fluid mechanics -- viscous flow within the fracture
  3. Material balance -- injected volume = fracture volume + leakoff volume
  4. Fracture mechanics -- propagation at the fracture tip

Common Parameters

Symbol Description Oilfield Units
QQ Injection rate (one wing) bbl/min
μ\mu Fracturing fluid viscosity cP
EE Young's modulus psi
ν\nu Poisson's ratio dimensionless
EE' Plane strain modulus, E=E/(1ν2)E' = E/(1-\nu^2) psi
hfh_f Fracture height ft
tt Pumping time min
CLC_L Carter leakoff coefficient ft/min$^{1/2}$
pnetp_{net} Net pressure (fracture pressure minus closure stress) psi
ww Fracture width (average or maximum) in
xfx_f Fracture half-length ft
RR Fracture radius (radial model) ft

Plane Strain Modulus

The plane strain modulus appears in all fracture width equations:

E=E1ν2E' = \frac{E}{1 - \nu^2}

Typical values:

  • Sandstone: E=16×106E = 1 - 6 \times 10^6 psi, ν=0.150.25\nu = 0.15 - 0.25
  • Shale: E=14×106E = 1 - 4 \times 10^6 psi, ν=0.250.35\nu = 0.25 - 0.35
  • Limestone: E=410×106E = 4 - 10 \times 10^6 psi, ν=0.250.30\nu = 0.25 - 0.30

PKN Model (Perkins-Kern-Nordgren)

Physical Description

The PKN model assumes:

  • Confined height: fracture height hfh_f is fixed by stress barriers above and below
  • Vertical plane strain: each vertical cross-section deforms independently
  • Length much greater than height: xfhfx_f \gg h_f
  • Elliptical cross-section: width varies elliptically across the height at any position along the length
  • Maximum width at wellbore: width decreases toward the fracture tip
    Plan View (top down)              Cross-Section at any x
    ┌─────────────────────┐           ┌────────────────┐
    │                     │           │    ◜      ◝    │ ▲
    │  ○                  │           │  ◜          ◝  │ │
    │ well  ──────────► tip           │◜     w(x)    ◝│ hf
    │  ○                  │           │  ◟          ◞  │ │
    │                     │           │    ◟      ◞    │ ▼
    └─────────────────────┘           └────────────────┘
    ◄────── xf ──────────►                ◄── w ──►
    Width decreases toward tip         Elliptical shape

Equations (No Leakoff)

Maximum width (at wellbore, x=0x = 0):

wmax=3.57(QμxfE)1/4w_{max} = 3.57 \left(\frac{Q \mu x_f}{E'}\right)^{1/4}

Where wmaxw_{max} is in inches when QQ is in bbl/min, μ\mu in cP, xfx_f in ft, and EE' in psi.

Fracture half-length (no leakoff, CL=0C_L = 0):

xf=0.524(EQ3μhf4)1/5t4/5x_f = 0.524 \left(\frac{E' Q^3}{\mu h_f^4}\right)^{1/5} t^{4/5}

Net pressure:

pnet=2.24(E3μQhf4)1/5t1/5p_{net} = 2.24 \left(\frac{E'^3 \mu Q}{h_f^4}\right)^{1/5} t^{1/5}

Note: In the PKN model, net pressure increases with time as the fracture grows longer and friction losses increase. This is a distinguishing diagnostic feature.

Fracture volume (one wing, average width = π/5×wmax\pi/5 \times w_{max}):

Vf=π5wmaxhfxfV_f = \frac{\pi}{5} w_{max} \cdot h_f \cdot x_f

Equations (With Carter Leakoff)

When leakoff is included, the half-length is reduced from the no-leakoff case. The Nordgren (1972) solution for fracture length with Carter leakoff uses the material balance:

xf=Qthf(wˉ+2πCLtg(η))x_f = \frac{Q t}{h_f \left(\bar{w} + 2 \pi C_L \sqrt{t} \cdot g(\eta)\right)}

Where g(η)g(\eta) is a function of fluid efficiency that accounts for the time-dependent exposure of fracture faces, and wˉ\bar{w} is the average fracture width.

For practical calculation, the length with leakoff is obtained iteratively from the material balance equation coupling width, length, and leakoff volume.

PKN Parameter Ranges

Parameter Typical Range Notes
xfx_f 200 -- 2,000 ft Limited by leakoff and pump time
wmaxw_{max} 0.2 -- 0.8 in Must exceed 3x proppant diameter
pnetp_{net} 100 -- 1,500 psi Increases during pumping
hfh_f 30 -- 200 ft Set by stress barriers

KGD Model (Khristianovic-Geertsma-de Klerk)

Physical Description

The KGD model assumes:

  • Confined height: fracture height hfh_f is fixed
  • Horizontal plane strain: deformation is uniform along the height
  • Length comparable to or less than height: xfhfx_f \leq h_f
  • Rectangular cross-section: width is constant along the height at any position
  • Maximum width at center: width is maximum at x=0x = 0 (center of length) and zero at the tips
    Plan View (top down)              Cross-Section at any x
    ┌─────────────────────┐           ┌────────────────┐
    │         tip         │           │                │ ▲
    │          │          │           │                │ │
    │  tip ── well ── tip │           │    w(x)        │ hf
    │          │          │           │   (uniform)    │ │
    │         tip         │           │                │ ▼
    └─────────────────────┘           └────────────────┘
    ◄────── xf ──────────►                ◄── w ──►
    Width max at center               Rectangular shape

Equations (No Leakoff)

Maximum width (at center of fracture, x=0x = 0):

wmax=3.22(Qμxf2Ehf)1/4w_{max} = 3.22 \left(\frac{Q \mu x_f^2}{E' h_f}\right)^{1/4}

Fracture half-length (no leakoff):

xf=0.539(EQ3μhf3)1/6t2/3x_f = 0.539 \left(\frac{E' Q^3}{\mu h_f^3}\right)^{1/6} t^{2/3}

Net pressure:

pnet=1.09(Eμ2Q2hf6)1/6t1/3p_{net} = 1.09 \left(\frac{E' \mu^2 Q^2}{h_f^6}\right)^{1/6} t^{-1/3}

Note: In the KGD model, net pressure decreases with time. This is opposite to the PKN model and serves as a diagnostic indicator.

Fracture volume (one wing, average width = π/4×wmax\pi/4 \times w_{max}):

Vf=π4wmaxhfxfV_f = \frac{\pi}{4} w_{max} \cdot h_f \cdot x_f

KGD Parameter Ranges

Parameter Typical Range Notes
xfx_f 50 -- 500 ft Shorter than PKN for same conditions
wmaxw_{max} 0.3 -- 1.0 in Wider than PKN for same conditions
pnetp_{net} 50 -- 500 psi Decreases during pumping
hfh_f 30 -- 200 ft Must be comparable to or greater than xfx_f

Radial (Penny-Shaped) Model

Physical Description

The radial model assumes:

  • No height confinement: fracture propagates radially from the wellbore
  • Circular (penny-shaped) geometry: fracture is a flat disk
  • Axial symmetry: width depends only on radial distance from center
  • Maximum width at center: width is maximum at the wellbore and zero at the circular tip

This model applies when stress barriers are absent or when the fracture has not yet reached confining layers (early time behavior).

    Plan View (top down)              Side View (cross-section)
         ╱────────╲
       ╱            ╲                 ────────────────────────
     ╱                ╲                  ◜                ◝
    │        ●         │              ◜         w(r)        ◝
     ╲      well      ╱                  ◟                ◞
       ╲            ╱                 ────────────────────────
         ╲────────╱
    ◄──────── R ────────►             ◄────────── R ──────────►
       Circular front                   Ellipsoidal opening

Equations (No Leakoff)

Maximum width (at wellbore center):

wmax=3.65(μQRE)1/4w_{max} = 3.65 \left(\frac{\mu Q R}{E'}\right)^{1/4}

Fracture radius (no leakoff):

R=0.572(EQ3μ)1/9t4/9R = 0.572 \left(\frac{E' Q^3}{\mu}\right)^{1/9} t^{4/9}

Net pressure:

pnet=2.51(E3μ5Q5R13)1/9p_{net} = 2.51 \left(\frac{E'^3 \mu^5 Q^5}{R^{13}}\right)^{1/9}

Or expressed in terms of time:

pnett1/3p_{net} \propto t^{-1/3}

Note: Like the KGD model, net pressure in the radial model decreases with time.

Fracture volume (average width = 8/(3π)×wmax8/(3\pi) \times w_{max}):

Vf=83πwmaxπR2=83wmaxR2V_f = \frac{8}{3\pi} w_{max} \cdot \pi R^2 = \frac{8}{3} w_{max} R^2

Radial Model Parameter Ranges

Parameter Typical Range Notes
RR 50 -- 500 ft Limited by eventual height confinement
wmaxw_{max} 0.1 -- 0.6 in Typically narrower than confined models
pnetp_{net} 50 -- 500 psi Decreases during pumping

Carter Leakoff Model

Theory

Carter (1957) described fluid loss from a fracture face with a time-dependent velocity:

uL(t,τ)=CLtτu_L(t, \tau) = \frac{C_L}{\sqrt{t - \tau}}

Where:

  • uLu_L = leakoff velocity normal to fracture face, ft/min
  • CLC_L = leakoff coefficient, ft/min$^{1/2}$
  • tt = current time, min
  • τ\tau = time when that fracture face element was first exposed

Leakoff Coefficient

The total leakoff coefficient combines three resistances in series:

Component Symbol Physical Mechanism
Filter-cake (wall-building) CIC_I Polymer residue on fracture face
Filtrate invasion CIIC_{II} Viscous filtrate displacing reservoir fluid
Reservoir compressibility CIIIC_{III} Pressure transient into formation

1CL=1CI+1Ceff\frac{1}{C_L} = \frac{1}{C_I} + \frac{1}{C_{eff}}

Where:

Ceff=CIICIIICII+CIII(1+1+(2CIICIIICII2+CIII2))÷2C_{eff} = \frac{C_{II} C_{III}}{C_{II} + C_{III}} \left(1 + \sqrt{1 + \left(\frac{2C_{II}C_{III}}{C_{II}^2 + C_{III}^2}\right)}\right) \div 2

In practice, the overall CLC_L is often determined directly from a mini-frac (diagnostic fracture injection test).

Typical Leakoff Coefficients

Formation CLC_L (ft/min$^{1/2}$) Character
Tight gas sand (k<0.01k < 0.01 mD) 0.0001 -- 0.001 Very low leakoff
Moderate sand (k=0.110k = 0.1 - 10 mD) 0.001 -- 0.01 Moderate leakoff
High-perm sand (k>50k > 50 mD) 0.01 -- 0.05 High leakoff

Cumulative Leakoff Volume

The total volume leaked off from one face of one wing over the fracture area:

VL=2hfCL0xftτ(x)dxV_L = 2 h_f C_L \int_0^{x_f} \sqrt{t - \tau(x)} \, dx

For a fracture with constant-rate propagation, this simplifies using the spurt loss and the leakoff area integral.

Fluid Efficiency

The fluid efficiency at any time is:

η=VfracVtotal=VfracVfrac+Vleakoff\eta = \frac{V_{frac}}{V_{total}} = \frac{V_{frac}}{V_{frac} + V_{leakoff}}

Where Vtotal=QtV_{total} = Q \cdot t (total pumped volume).

Material balance for the fracture at time tt:

Qt=Vfrac+Vleakoff+VspurtQ t = V_{frac} + V_{leakoff} + V_{spurt}

Rearranging:

η=1Vleakoff+VspurtQt\eta = 1 - \frac{V_{leakoff} + V_{spurt}}{Q t}


Model Comparison

Assumptions Summary

Assumption PKN KGD Radial
Height fixed Yes Yes No
Plane strain direction Vertical Horizontal Axial
Cross-section shape Elliptical Rectangular Ellipsoidal
Width varies along height Yes (elliptical) No (uniform) Yes (radial)
Width varies along length Yes (max at well) Yes (max at center) Yes (max at center)
Length/height ratio xf/hf>1x_f / h_f > 1 xf/hf1x_f / h_f \leq 1 N/A
Tip condition No tip singularity Stress intensity Stress intensity

Scaling Laws (No Leakoff)

Quantity PKN KGD Radial
Length/Radius \propto t4/5t^{4/5} t2/3t^{2/3} t4/9t^{4/9}
Width \propto t1/5t^{1/5} t1/6t^{1/6} t1/9t^{1/9}
Net pressure \propto t1/5t^{1/5} (increasing) t1/3t^{-1/3} (decreasing) t1/3t^{-1/3} (decreasing)
Volume \propto t1t^{1} t1t^{1} t1t^{1}

When to Use Each Model

Scenario Recommended Model Rationale
Long fracture in thin pay PKN xfhfx_f \gg h_f, strong barriers
Short treatment, thick zone KGD xfhfx_f \leq h_f, horizontal strain
No stress barriers Radial Unconstrained height growth
Early pumping (any case) Radial Before fracture reaches barriers
Design optimization PKN Most common field scenario
Laboratory experiments KGD Short fractures in blocks

Net Pressure Diagnostic

The trend of net pressure during pumping indicates which model governs:

log(p_net)
    │
    │     ╱                PKN: slope = +1/5
    │   ╱
    │ ╱
    │╱─────────────────    Transition
    │╲
    │  ╲                   KGD/Radial: slope = -1/3
    │    ╲
    └──────────────────→ log(t)
  • Rising net pressure: PKN behavior (fracture lengthening, increasing friction)
  • Falling net pressure: KGD or Radial behavior (fracture widening, decreasing resistance)
  • Flat net pressure: Equilibrium or height growth (not captured by 2D models)


References

  1. Perkins, T.K. and Kern, L.R. (1961). "Widths of Hydraulic Fractures." Journal of Petroleum Technology, 13(9), pp. 937-949. SPE-89-PA.

  2. Nordgren, R.P. (1972). "Propagation of a Vertical Hydraulic Fracture." Society of Petroleum Engineers Journal, 12(4), pp. 306-314. SPE-3009-PA.

  3. Geertsma, J. and de Klerk, F. (1969). "A Rapid Method of Predicting Width and Extent of Hydraulically Induced Fractures." Journal of Petroleum Technology, 21(12), pp. 1571-1581. SPE-2458-PA.

  4. Carter, R.D. (1957). "Derivation of the General Equation for Estimating the Extent of the Fractured Area." Appendix to: Howard, G.C. and Fast, C.R., "Optimum Fluid Characteristics for Fracture Extension." Drilling and Production Practice, API, pp. 261-270.

  5. Sneddon, I.N. (1946). "The Distribution of Stress in the Neighbourhood of a Crack in an Elastic Solid." Proceedings of the Royal Society A, 187(1009), pp. 229-260.

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