Run any Skill in Manus with one click

Get Started

turbulence-models-db

Select and configure turbulence models (k-epsilon, k-omega SST, LES) for CFD

Run Skill in Manus

Overview

Select and configure turbulence models (k-epsilon, k-omega SST, LES) for CFD

Install command

npx skills add https://github.com/Soljourner/claude-engineering-skills --skill turbulence-models-db

Copy and paste this command into Claude Code to install the skill

Source

Soljourner/claude-engineering-skills

Stars20

Forks7

UpdatedNovember 7, 2025 at 22:15

File Explorer

2 files

SKILL.md

readonly

Turbulence Models Database

A comprehensive reference for selecting and configuring turbulence models in computational fluid dynamics (CFD) simulations.

Overview of Turbulence Modeling

Turbulence is a chaotic, three-dimensional, time-dependent flow phenomenon characterized by random fluctuations in velocity, pressure, and other flow quantities. Direct numerical simulation (DNS) of turbulent flows is computationally prohibitive for most engineering applications, necessitating turbulence modeling approaches.

Modeling Approaches Hierarchy

DNS (Direct Numerical Simulation): Resolves all turbulent scales, no modeling
LES (Large Eddy Simulation): Resolves large scales, models small scales
RANS (Reynolds-Averaged Navier-Stokes): Models all turbulent scales
Laminar: No turbulence modeling

RANS Turbulence Models

RANS models solve time-averaged equations and model turbulent fluctuations using the Reynolds stress concept. They are the most widely used in industrial CFD due to computational efficiency.

k-ε Models (k-epsilon)

The k-ε family models turbulent kinetic energy (k) and its dissipation rate (ε).

Standard k-ε

Characteristics:

Two-equation model
Robust and widely validated
Good for free shear flows and fully turbulent flows
Poor for flows with strong adverse pressure gradients
Not suitable for low-Reynolds number flows without modifications

Best Applications:

Fully turbulent flows
Free shear layers, mixing layers, jets
Flow in ducts and channels (far from walls)
Industrial flows with high Reynolds numbers

Limitations:

Overpredicts separation
Poor near-wall performance without wall functions
Inaccurate for swirling flows
Stagnation point anomaly

Wall Treatment:

Requires y+ > 30 (typically 30-300) with wall functions
Not suitable for wall-resolved simulations

RNG k-ε

Characteristics:

Derived using Renormalization Group theory
Improved performance for swirling flows and streamline curvature
Better handles low-Reynolds number effects
Modified ε equation improves accuracy for rapidly strained flows

Best Applications:

Flows with strong streamline curvature
Swirling and rotating flows
Transitional flows (with enhanced wall treatment)
Separated flows (better than standard k-ε)

Improvements over Standard k-ε:

Additional term in ε equation for rapid strain
Modified turbulent viscosity formula
Better prediction of near-wall flows

Wall Treatment:

Can use wall functions (y+ > 30)
Enhanced wall treatment allows y+ ≈ 1

Realizable k-ε

Characteristics:

Ensures mathematical realizability constraints
Variable Cμ coefficient
Improved prediction of spreading rate for planar and round jets
Better performance for rotating flows and boundary layers under strong adverse pressure gradients

Best Applications:

Flows with rotation and recirculation
Boundary layers with strong pressure gradients
Separated flows
Jets and mixing layers

Advantages:

More accurate for complex flows than standard k-ε
Superior prediction of jet spreading rates
Better captures effects of streamline curvature

Wall Treatment:

Standard wall functions (y+ > 30)
Enhanced wall treatment available (y+ ≈ 1)

k-ω Models (k-omega)

The k-ω family models turbulent kinetic energy (k) and specific dissipation rate (ω).

Standard k-ω (Wilcox)

Characteristics:

Two-equation model
Superior near-wall treatment without wall functions
Accurate for adverse pressure gradients
Sensitive to freestream values of ω
Good for transitional flows

Best Applications:

Low-Reynolds number flows
Transitional flows
Flows with adverse pressure gradients
Aerodynamic flows (airfoils, wings)
Wall-bounded flows

Limitations:

Highly sensitive to freestream ω values
Less accurate in free shear flows compared to k-ε
Can be numerically stiff

Wall Treatment:

Integrates to the wall (y+ ≈ 1 required)
No wall functions needed for near-wall region

k-ω SST (Shear Stress Transport)

Characteristics:

Blends k-ω near walls with k-ε in freestream
Insensitive to freestream values
Accounts for transport of turbulent shear stress
Modified turbulent viscosity formulation
Industry standard for aerodynamics

Best Applications:

Aerodynamic flows (external aerodynamics)
Flows with adverse pressure gradients and separation
Transonic flows
Heat transfer problems
Turbomachinery

Advantages:

Combines strengths of k-ω (near-wall) and k-ε (far-field)
Accurate separation prediction
Not sensitive to freestream turbulence values
Robust and reliable

Limitations:

Requires fine near-wall mesh (y+ ≈ 1)
More computationally expensive than standard models
Can underpredict separation in some cases

Wall Treatment:

Designed for low-Reynolds number (y+ ≈ 1)
Automatic wall functions available for coarse meshes
Best results with wall-resolved mesh

Spalart-Allmaras

Characteristics:

One-equation model (solves for modified turbulent viscosity)
Designed for aerodynamic flows
Low computational cost
Good for wall-bounded flows
Limited for free shear flows and decaying turbulence

Best Applications:

Aerospace applications
External aerodynamics (airfoils, wings, fuselages)
Mild separation and attached flows
Transonic flows

Advantages:

Computationally efficient (one equation)
Robust and stable
Good near-wall behavior
Well-suited for structured meshes

Limitations:

Not suitable for complex flows with multiple physics
Limited accuracy for free shear flows
Not ideal for internal flows
Poor for flows with large separation regions

Wall Treatment:

Designed for low-Reynolds number (y+ ≈ 1)
Can use wall functions for coarser meshes

Reynolds Stress Models (RSM)

Characteristics:

Seven-equation model (6 Reynolds stresses + ε or ω)
Solves transport equations for each Reynolds stress component
Accounts for anisotropy of turbulence
Most complex RANS approach

Best Applications:

Highly swirling flows
Flows with strong streamline curvature
Complex 3D flows
Rotating flows and cyclone separators
Flows where turbulence anisotropy is critical

Advantages:

Most accurate RANS model for complex flows
Captures turbulence anisotropy
No isotropic eddy viscosity assumption

Limitations:

Most computationally expensive RANS model
Convergence can be challenging
Requires very good mesh quality
More sensitive to numerical settings

Large Eddy Simulation (LES)

Overview

LES resolves large turbulent eddies directly while modeling small-scale (subgrid-scale) turbulence. Provides time-accurate flow structures.

Characteristics:

Spatially filtered Navier-Stokes equations
Resolves energy-containing eddies
Models universal small-scale turbulence
Requires 3D time-dependent simulation

Mesh Requirements:

Very fine mesh (Δx, Δy, Δz ≈ local turbulent length scale)
Isotropic or near-isotropic cells in turbulent regions
y+ < 1 for wall-resolved LES
Wall-modeled LES: y+ can be 30-100

Computational Cost:

10-100x more expensive than RANS
Scales as Re^(9/4) for channel flows
Requires long simulation times for statistical convergence

Subgrid-Scale Models

Smagorinsky-Lilly

Classic algebraic model
Cs ≈ 0.1-0.2 (model constant)
Overly dissipative near walls

Dynamic Smagorinsky

Computes Cs dynamically
More accurate than standard Smagorinsky
Self-adapting to flow conditions

WALE (Wall-Adapting Local Eddy-viscosity)

Better near-wall behavior
Returns correct y³ scaling near walls
No dynamic procedure needed

Kinetic Energy Subgrid-Scale

One-equation model for subgrid kinetic energy
More accurate but more expensive

Applications of LES

Best suited for:

Acoustics (noise prediction)
Combustion and reacting flows
Complex unsteady flows
Flows with large-scale instabilities
Vortex shedding and wake flows
Mixing problems

Not recommended for:

Steady-state problems
High-Reynolds number wall-bounded flows (prohibitive cost)
Industrial simulations with limited resources

Hybrid RANS-LES Methods

DES (Detached Eddy Simulation)

RANS near walls, LES in separated regions
Good for massively separated flows
More affordable than pure LES

DDES (Delayed DES)

Improved shielding of boundary layer
Prevents premature switch to LES mode

SDES (Shielded DES)

Further improvements to RANS-LES interface
Better suited for attached flows

SAS (Scale-Adaptive Simulation)

RANS-based but resolves large unsteady structures
Automatic adjustment to resolved scales

Model Selection Criteria

Flow Type Classification

Internal Flows

Examples: Pipes, ducts, channels, valves, pumps Recommended models:

k-ε Realizable (general purpose)
k-ω SST (with heat transfer or separation)
Standard k-ε (simple fully turbulent)

External Flows

Examples: Airfoils, vehicles, buildings, external aerodynamics Recommended models:

k-ω SST (industry standard)
Spalart-Allmaras (aerospace)
Realizable k-ε (blunt bodies)

Free Shear Flows

Examples: Jets, wakes, mixing layers Recommended models:

Realizable k-ε
Standard k-ε
RNG k-ε

Separated Flows

Examples: Flow over backward-facing step, airfoil stall Recommended models:

k-ω SST (best for mild-moderate separation)
DES/DDES (massive separation)
LES (if resources available)

Rotating/Swirling Flows

Examples: Turbomachinery, cyclones, swirl burners Recommended models:

RNG k-ε
RSM
k-ω SST

Reynolds Number Considerations

Low Re (Re < 10⁴):

Low-Re k-ω or k-ω SST
Spalart-Allmaras
May need transitional models

Moderate Re (10⁴ < Re < 10⁶):

Most RANS models applicable
k-ω SST for aerodynamics
Realizable k-ε for internal flows

High Re (Re > 10⁶):

Standard k-ε (with wall functions)
k-ω SST
Realizable k-ε

Very High Re (Re > 10⁷):

Wall function approaches necessary
Standard k-ε
Realizable k-ε

Mesh Requirements and y+ Values

Wall Functions Approach

y+ range: 30 < y+ < 300 (ideally 30-100) Models:

Standard k-ε
Realizable k-ε
RNG k-ε (with standard wall functions)

Advantages:

Coarser mesh acceptable
Lower computational cost
Suitable for high-Re flows

Limitations:

Less accurate near-wall gradients
Not suitable for low-Re or transitional flows
Poor for flows with separation or reattachment

Wall-Resolved Approach

y+ range: y+ ≈ 1 (first cell) Models:

k-ω SST
Standard k-ω
Spalart-Allmaras
Low-Re k-ε variants

Requirements:

Very fine near-wall mesh
At least 10-15 cells in boundary layer
y+ < 1 for first cell
Growth ratio ≤ 1.2 near wall

Advantages:

Accurate near-wall resolution
Captures boundary layer accurately
Better for heat transfer
Handles low-Re and transitional flows

Limitations:

High cell count
Increased computational cost
Mesh generation more complex

Enhanced Wall Treatment

y+ range: y+ < 5 or 30 < y+ < 300 (adaptive) Models:

Realizable k-ε with EWT
RNG k-ε with EWT

Advantages:

Flexibility in mesh resolution
Blends wall functions and low-Re formulation
Handles variable y+ in domain

y+ Guidelines by Application

Application	Target y+	Model Recommendation
External aerodynamics	y+ ≈ 1	k-ω SST
Heat transfer	y+ < 1	k-ω SST, Low-Re
Turbomachinery	y+ ≈ 1-2	k-ω SST
Internal flows (simple)	y+ = 30-100	Realizable k-ε
Separation prediction	y+ ≈ 1	k-ω SST
High-speed flows	y+ ≈ 1	k-ω SST, SA
LES wall-resolved	y+ < 1	LES with WALE/Dynamic
LES wall-modeled	y+ = 30-100	WMLES

Computational Cost Comparison

Relative cost (normalized to standard k-ε = 1):

Model	Relative Cost	Memory	Convergence
Spalart-Allmaras	0.8	Low	Good
Standard k-ε	1.0	Low	Excellent
RNG k-ε	1.1	Low	Good
Realizable k-ε	1.1	Low	Good
Standard k-ω	1.2	Low	Fair
k-ω SST	1.3	Low	Good
RSM	2.0-2.5	Medium	Fair-Poor
DES/DDES	5-20	High	Fair
LES	50-500	Very High	N/A (time-accurate)

Model Constants and Parameters

Standard k-ε Constants

Cμ = 0.09
C1ε = 1.44
C2ε = 1.92
σk = 1.0
σε = 1.3

RNG k-ε Constants

Cμ = 0.0845
C1ε = 1.42
C2ε = 1.68
σk = 0.7179
σε = 0.7179
η0 = 4.38
β = 0.012

Realizable k-ε Constants

C1ε = 1.44
C2 = 1.9
σk = 1.0
σε = 1.2
Cμ = variable (function of strain rate and rotation)

Standard k-ω Constants

α = 5/9
β = 0.075
β* = 0.09
σk = 2.0
σω = 2.0

k-ω SST Constants

k-ω inner:

α1 = 5/9
β1 = 0.075
σk1 = 2.0
σω1 = 2.0

k-ε outer (transformed):

α2 = 0.44
β2 = 0.0828
σk2 = 1.0
σω2 = 1.168

Other:

β* = 0.09
a1 = 0.31 (SST limiter constant)

Spalart-Allmaras Constants

cb1 = 0.1355
cb2 = 0.622
σ = 2/3
κ = 0.41 (von Karman constant)
cw1 = cb1/κ² + (1 + cb2)/σ
cw2 = 0.3
cw3 = 2.0
cv1 = 7.1

Wall Functions vs Wall-Resolved

Standard Wall Functions

Theory:

Based on law of the wall
Assumes equilibrium boundary layer
Logarithmic law: u+ = (1/κ)ln(y+) + B

Requirements:

30 < y+ < 300
Equilibrium turbulent boundary layer
No significant pressure gradients

When to use:

High-Re fully turbulent flows
Simple geometries
Limited computational resources
Steady-state simulations

Limitations:

Inaccurate for adverse pressure gradients
Poor for separation and reattachment
Not suitable for heat transfer predictions
Fails in transitional flows

Scalable Wall Functions

Improvements:

Avoid deterioration for fine meshes
y+ insensitive formulation
Better for y+ < 30

Non-Equilibrium Wall Functions

Improvements:

Account for pressure gradient effects
Improved separation prediction
Better suited for complex flows

When to use:

Flows with pressure gradients
Separation and reattachment
Complex geometries

Enhanced Wall Treatment (EWT)

Characteristics:

Two-layer approach
Blends wall functions (high y+) with low-Re formulation (low y+)
Adaptive based on local y+

When to use:

Variable mesh resolution
Uncertainty in y+ values
Complex geometries with varying resolution

Wall-Resolved (Low-Re)

Requirements:

y+ ≈ 1 (ideally y+ < 1)
10-15+ cells in boundary layer
Growth ratio ≤ 1.2 near wall
Integration to wall (no wall functions)

When to use:

Accurate heat transfer required
Separation prediction critical
Low-Re or transitional flows
Aerodynamic design optimization

Models requiring wall-resolved:

k-ω SST (optimal)
Standard k-ω
Spalart-Allmaras (optimal)
LES

Turbulence Model Selection Decision Tree

START: What is your flow problem?
│
├─ Need time-accurate unsteady structures?
│  │
│  ├─ YES: Go to LES/Hybrid
│  │  │
│  │  ├─ Can afford very fine mesh and long run time?
│  │  │  ├─ YES: LES (wall-resolved or wall-modeled)
│  │  │  └─ NO: DES/DDES (massively separated flows) or SAS
│  │  │
│  │  └─ Is flow primarily attached?
│  │     ├─ YES: URANS (k-ω SST or Realizable k-ε)
│  │     └─ NO: DES/DDES
│  │
│  └─ NO: Continue to RANS selection
│
├─ Flow type?
│  │
│  ├─ External aerodynamics (airfoils, vehicles, aircraft)
│  │  └─ k-ω SST (first choice) or Spalart-Allmaras
│  │     Required: y+ ≈ 1, wall-resolved mesh
│  │
│  ├─ Internal flows (pipes, ducts, channels)
│  │  │
│  │  ├─ Heat transfer important?
│  │  │  ├─ YES: k-ω SST (y+ ≈ 1)
│  │  │  └─ NO: Continue
│  │  │
│  │  ├─ Separation or adverse pressure gradients?
│  │  │  ├─ YES: k-ω SST (y+ ≈ 1) or Realizable k-ε (EWT)
│  │  │  └─ NO: Realizable k-ε (wall functions, y+ = 30-100)
│  │  │
│  │  └─ Simple fully turbulent?
│  │     └─ Standard k-ε (wall functions, y+ = 30-100)
│  │
│  ├─ Free shear flows (jets, wakes, mixing)
│  │  └─ Realizable k-ε or RNG k-ε
│  │
│  ├─ Rotating/swirling flows (turbomachinery, cyclones)
│  │  │
│  │  ├─ Simple rotation?
│  │  │  └─ RNG k-ε or k-ω SST
│  │  │
│  │  └─ Complex 3D rotation with strong curvature?
│  │     └─ RSM (if resources available) or RNG k-ε
│  │
│  └─ Separated flows (backward step, airfoil stall)
│     │
│     ├─ Mild-moderate separation?
│     │  └─ k-ω SST (y+ ≈ 1)
│     │
│     └─ Massive separation?
│        └─ DES/DDES or LES (if affordable)
│
├─ Can you achieve y+ ≈ 1 near walls?
│  │
│  ├─ YES: k-ω SST, Spalart-Allmaras, or Low-Re k-ε
│  │
│  └─ NO: Must use wall functions
│     └─ Realizable k-ε or RNG k-ε (with EWT if possible)
│
└─ Special considerations:
   │
   ├─ Transitional flows (low Re)? → k-ω SST + transition model
   ├─ Compressible/high-speed? → k-ω SST or Spalart-Allmaras
   ├─ Buoyancy-driven? → Realizable k-ε or k-ω SST with buoyancy terms
   ├─ Multiphase flows? → Realizable k-ε or k-ω SST
   └─ Limited resources? → Standard k-ε or Spalart-Allmaras

Quick Selection Guide by Application

Aerospace

Model: k-ω SST or Spalart-Allmaras y+: ≈ 1 Rationale: Accurate prediction of boundary layers, separation, and pressure distribution

Automotive (External)

Model: k-ω SST y+: ≈ 1 Rationale: Separation prediction, drag/lift accuracy

HVAC / Building Ventilation

Model: Realizable k-ε with wall functions y+: 30-100 Rationale: Large domains, computational efficiency, adequate accuracy

Turbomachinery

Model: k-ω SST y+: 1-2 Rationale: Adverse pressure gradients, rotation, heat transfer

Combustion

Model: Realizable k-ε or LES y+: Depends (wall functions for RANS, y+ < 1 for LES) Rationale: Mixing, turbulence-chemistry interaction

Heat Exchangers

Model: k-ω SST or Realizable k-ε with EWT y+: < 5 or wall-resolved Rationale: Heat transfer accuracy critical

Mixing / Chemical Reactors

Model: Realizable k-ε or RSM y+: 30-100 Rationale: Capturing mixing patterns, turbulence anisotropy

Hydraulics (Dams, Spillways)

Model: Realizable k-ε or k-ω SST y+: Variable Rationale: Free surface flows, separation, aeration

Environmental (Atmospheric flows)

Model: Standard k-ε or Realizable k-ε y+: Wall functions Rationale: Large scale, computational cost, atmospheric boundary layer

Best Practices

General Guidelines

Start simple: Begin with simpler models (k-ε, k-ω SST) before trying complex models
Validate mesh: Ensure y+ values are appropriate for chosen model
Check mesh quality: Turbulence models are sensitive to mesh quality
Monitor residuals: Turbulence equations often converge slower than momentum
Use appropriate boundary conditions: Turbulent intensity and length scale matter
Verify sensitivity: Test mesh independence and model sensitivity

Boundary Conditions

Inlet:

Turbulent intensity: I = 0.16 Re^(-1/8) for fully developed pipe flow
Low turbulence: I = 0.1% - 1%
Medium turbulence: I = 1% - 5%
High turbulence: I = 5% - 20%
Turbulent length scale: l ≈ 0.07 × characteristic length

Wall:

No-slip condition
Wall functions or wall-resolved (model dependent)
Roughness can be specified (equivalent sand-grain roughness)

Outlet:

Zero gradient (outflow)
Fixed pressure

Convergence Tips

Initialize properly: Use potential flow or previous solution
Under-relax initially: Start with URF = 0.3-0.5 for turbulence equations
Gradually increase: Increase URF as solution stabilizes
Coupled solvers: Often help with k-ω models
Monitor flow features: Check separation, reattachment, vortex shedding
Residuals alone insufficient: Verify force/flux convergence

Common Pitfalls

Incorrect y+: Most common error; check and adjust mesh
Poor mesh quality: High skewness, aspect ratio issues
Inadequate refinement: In regions of high gradients
Wrong model for application: Using k-ε for separated flows
Freestream sensitivity: k-ω without SST correction
Ignoring validation: Always compare with experiments or benchmarks

Summary Table: RANS Model Comparison

Model	Equations	y+ Requirement	Best For	Avoid For	Computational Cost
Standard k-ε	2	30-300	Simple internal flows, fully turbulent	Separation, low-Re, adverse pressure gradients	Low
RNG k-ε	2	30-300 (or EWT)	Swirl, rotation, moderate separation	Simple flows (overkill)	Low-Medium
Realizable k-ε	2	30-300 (or EWT)	Complex flows, jets, separation, general purpose	Critical aerodynamics	Low-Medium
Standard k-ω	2	≈ 1	Low-Re, transitional, near-wall	Freestream flows (sensitive to ω∞)	Medium
k-ω SST	2	≈ 1	Aerodynamics, separation, adverse pressure gradients	Simple internal flows (expensive)	Medium
Spalart-Allmaras	1	≈ 1	Aerospace, external aerodynamics, mild separation	Internal flows, free shear, complex physics	Low
RSM	7	≈ 1 or 30-300	Anisotropic turbulence, strong swirl, complex 3D	Simple flows, limited resources	High

References

See reference.md for detailed equations, validation cases, and academic references.

name	turbulence-models-db
description	Select and configure turbulence models (k-epsilon, k-omega SST, LES) for CFD
category	databases
domain	fluids
complexity	advanced
dependencies	[]

Turbulence Models Database

A comprehensive reference for selecting and configuring turbulence models in computational fluid dynamics (CFD) simulations.

Overview of Turbulence Modeling

Modeling Approaches Hierarchy

DNS (Direct Numerical Simulation): Resolves all turbulent scales, no modeling
LES (Large Eddy Simulation): Resolves large scales, models small scales
RANS (Reynolds-Averaged Navier-Stokes): Models all turbulent scales
Laminar: No turbulence modeling

RANS Turbulence Models

RANS models solve time-averaged equations and model turbulent fluctuations using the Reynolds stress concept. They are the most widely used in industrial CFD due to computational efficiency.

k-ε Models (k-epsilon)

The k-ε family models turbulent kinetic energy (k) and its dissipation rate (ε).

Standard k-ε

Characteristics:

Two-equation model
Robust and widely validated
Good for free shear flows and fully turbulent flows
Poor for flows with strong adverse pressure gradients
Not suitable for low-Reynolds number flows without modifications

Best Applications:

Fully turbulent flows
Free shear layers, mixing layers, jets
Flow in ducts and channels (far from walls)
Industrial flows with high Reynolds numbers

Limitations:

Overpredicts separation
Poor near-wall performance without wall functions
Inaccurate for swirling flows
Stagnation point anomaly

Wall Treatment:

Requires y+ > 30 (typically 30-300) with wall functions
Not suitable for wall-resolved simulations

RNG k-ε

Characteristics:

Derived using Renormalization Group theory
Improved performance for swirling flows and streamline curvature
Better handles low-Reynolds number effects
Modified ε equation improves accuracy for rapidly strained flows

Best Applications:

Flows with strong streamline curvature
Swirling and rotating flows
Transitional flows (with enhanced wall treatment)
Separated flows (better than standard k-ε)

Improvements over Standard k-ε:

Additional term in ε equation for rapid strain
Modified turbulent viscosity formula
Better prediction of near-wall flows

Wall Treatment:

Can use wall functions (y+ > 30)
Enhanced wall treatment allows y+ ≈ 1

Realizable k-ε

Characteristics:

Ensures mathematical realizability constraints
Variable Cμ coefficient
Improved prediction of spreading rate for planar and round jets
Better performance for rotating flows and boundary layers under strong adverse pressure gradients

Best Applications:

Flows with rotation and recirculation
Boundary layers with strong pressure gradients
Separated flows
Jets and mixing layers

Advantages:

More accurate for complex flows than standard k-ε
Superior prediction of jet spreading rates
Better captures effects of streamline curvature

Wall Treatment:

Standard wall functions (y+ > 30)
Enhanced wall treatment available (y+ ≈ 1)

k-ω Models (k-omega)

The k-ω family models turbulent kinetic energy (k) and specific dissipation rate (ω).

Standard k-ω (Wilcox)

Characteristics:

Two-equation model
Superior near-wall treatment without wall functions
Accurate for adverse pressure gradients
Sensitive to freestream values of ω
Good for transitional flows

Best Applications:

Low-Reynolds number flows
Transitional flows
Flows with adverse pressure gradients
Aerodynamic flows (airfoils, wings)
Wall-bounded flows

Limitations:

Highly sensitive to freestream ω values
Less accurate in free shear flows compared to k-ε
Can be numerically stiff

Wall Treatment:

Integrates to the wall (y+ ≈ 1 required)
No wall functions needed for near-wall region

k-ω SST (Shear Stress Transport)

Characteristics:

Blends k-ω near walls with k-ε in freestream
Insensitive to freestream values
Accounts for transport of turbulent shear stress
Modified turbulent viscosity formulation
Industry standard for aerodynamics

Best Applications:

Aerodynamic flows (external aerodynamics)
Flows with adverse pressure gradients and separation
Transonic flows
Heat transfer problems
Turbomachinery

Advantages:

Combines strengths of k-ω (near-wall) and k-ε (far-field)
Accurate separation prediction
Not sensitive to freestream turbulence values
Robust and reliable

Limitations:

Requires fine near-wall mesh (y+ ≈ 1)
More computationally expensive than standard models
Can underpredict separation in some cases

Wall Treatment:

Designed for low-Reynolds number (y+ ≈ 1)
Automatic wall functions available for coarse meshes
Best results with wall-resolved mesh

Spalart-Allmaras

Characteristics:

One-equation model (solves for modified turbulent viscosity)
Designed for aerodynamic flows
Low computational cost
Good for wall-bounded flows
Limited for free shear flows and decaying turbulence

Best Applications:

Aerospace applications
External aerodynamics (airfoils, wings, fuselages)
Mild separation and attached flows
Transonic flows

Advantages:

Computationally efficient (one equation)
Robust and stable
Good near-wall behavior
Well-suited for structured meshes

Limitations:

Not suitable for complex flows with multiple physics
Limited accuracy for free shear flows
Not ideal for internal flows
Poor for flows with large separation regions

Wall Treatment:

Designed for low-Reynolds number (y+ ≈ 1)
Can use wall functions for coarser meshes

Reynolds Stress Models (RSM)

Characteristics:

Seven-equation model (6 Reynolds stresses + ε or ω)
Solves transport equations for each Reynolds stress component
Accounts for anisotropy of turbulence
Most complex RANS approach

Best Applications:

Highly swirling flows
Flows with strong streamline curvature
Complex 3D flows
Rotating flows and cyclone separators
Flows where turbulence anisotropy is critical

Advantages:

Most accurate RANS model for complex flows
Captures turbulence anisotropy
No isotropic eddy viscosity assumption

Limitations:

Most computationally expensive RANS model
Convergence can be challenging
Requires very good mesh quality
More sensitive to numerical settings

Large Eddy Simulation (LES)

Overview

LES resolves large turbulent eddies directly while modeling small-scale (subgrid-scale) turbulence. Provides time-accurate flow structures.

Characteristics:

Spatially filtered Navier-Stokes equations
Resolves energy-containing eddies
Models universal small-scale turbulence
Requires 3D time-dependent simulation

Mesh Requirements:

Very fine mesh (Δx, Δy, Δz ≈ local turbulent length scale)
Isotropic or near-isotropic cells in turbulent regions
y+ < 1 for wall-resolved LES
Wall-modeled LES: y+ can be 30-100

Computational Cost:

10-100x more expensive than RANS
Scales as Re^(9/4) for channel flows
Requires long simulation times for statistical convergence

Subgrid-Scale Models

Smagorinsky-Lilly

Classic algebraic model
Cs ≈ 0.1-0.2 (model constant)
Overly dissipative near walls

Dynamic Smagorinsky

Computes Cs dynamically
More accurate than standard Smagorinsky
Self-adapting to flow conditions

WALE (Wall-Adapting Local Eddy-viscosity)

Better near-wall behavior
Returns correct y³ scaling near walls
No dynamic procedure needed

Kinetic Energy Subgrid-Scale

One-equation model for subgrid kinetic energy
More accurate but more expensive

Applications of LES

Best suited for:

Acoustics (noise prediction)
Combustion and reacting flows
Complex unsteady flows
Flows with large-scale instabilities
Vortex shedding and wake flows
Mixing problems

Not recommended for:

Steady-state problems
High-Reynolds number wall-bounded flows (prohibitive cost)
Industrial simulations with limited resources

Hybrid RANS-LES Methods

DES (Detached Eddy Simulation)

RANS near walls, LES in separated regions
Good for massively separated flows
More affordable than pure LES

DDES (Delayed DES)

Improved shielding of boundary layer
Prevents premature switch to LES mode

SDES (Shielded DES)

Further improvements to RANS-LES interface
Better suited for attached flows

SAS (Scale-Adaptive Simulation)

RANS-based but resolves large unsteady structures
Automatic adjustment to resolved scales

Model Selection Criteria

Flow Type Classification

Internal Flows

Examples: Pipes, ducts, channels, valves, pumps Recommended models:

k-ε Realizable (general purpose)
k-ω SST (with heat transfer or separation)
Standard k-ε (simple fully turbulent)

External Flows

Examples: Airfoils, vehicles, buildings, external aerodynamics Recommended models:

k-ω SST (industry standard)
Spalart-Allmaras (aerospace)
Realizable k-ε (blunt bodies)

Free Shear Flows

Examples: Jets, wakes, mixing layers Recommended models:

Realizable k-ε
Standard k-ε
RNG k-ε

Separated Flows

Examples: Flow over backward-facing step, airfoil stall Recommended models:

k-ω SST (best for mild-moderate separation)
DES/DDES (massive separation)
LES (if resources available)

Rotating/Swirling Flows

Examples: Turbomachinery, cyclones, swirl burners Recommended models:

RNG k-ε
RSM
k-ω SST

Reynolds Number Considerations

Low Re (Re < 10⁴):

Low-Re k-ω or k-ω SST
Spalart-Allmaras
May need transitional models

Moderate Re (10⁴ < Re < 10⁶):

Most RANS models applicable
k-ω SST for aerodynamics
Realizable k-ε for internal flows

High Re (Re > 10⁶):

Standard k-ε (with wall functions)
k-ω SST
Realizable k-ε

Very High Re (Re > 10⁷):

Wall function approaches necessary
Standard k-ε
Realizable k-ε

Mesh Requirements and y+ Values

Wall Functions Approach

y+ range: 30 < y+ < 300 (ideally 30-100) Models:

Standard k-ε
Realizable k-ε
RNG k-ε (with standard wall functions)

Advantages:

Coarser mesh acceptable
Lower computational cost
Suitable for high-Re flows

Limitations:

Less accurate near-wall gradients
Not suitable for low-Re or transitional flows
Poor for flows with separation or reattachment

Wall-Resolved Approach

y+ range: y+ ≈ 1 (first cell) Models:

k-ω SST
Standard k-ω
Spalart-Allmaras
Low-Re k-ε variants

Requirements:

Very fine near-wall mesh
At least 10-15 cells in boundary layer
y+ < 1 for first cell
Growth ratio ≤ 1.2 near wall

Advantages:

Accurate near-wall resolution
Captures boundary layer accurately
Better for heat transfer
Handles low-Re and transitional flows

Limitations:

High cell count
Increased computational cost
Mesh generation more complex

Enhanced Wall Treatment

y+ range: y+ < 5 or 30 < y+ < 300 (adaptive) Models:

Realizable k-ε with EWT
RNG k-ε with EWT

Advantages:

Flexibility in mesh resolution
Blends wall functions and low-Re formulation
Handles variable y+ in domain

y+ Guidelines by Application

Application	Target y+	Model Recommendation
External aerodynamics	y+ ≈ 1	k-ω SST
Heat transfer	y+ < 1	k-ω SST, Low-Re
Turbomachinery	y+ ≈ 1-2	k-ω SST
Internal flows (simple)	y+ = 30-100	Realizable k-ε
Separation prediction	y+ ≈ 1	k-ω SST
High-speed flows	y+ ≈ 1	k-ω SST, SA
LES wall-resolved	y+ < 1	LES with WALE/Dynamic
LES wall-modeled	y+ = 30-100	WMLES

Computational Cost Comparison

Relative cost (normalized to standard k-ε = 1):

Model	Relative Cost	Memory	Convergence
Spalart-Allmaras	0.8	Low	Good
Standard k-ε	1.0	Low	Excellent
RNG k-ε	1.1	Low	Good
Realizable k-ε	1.1	Low	Good
Standard k-ω	1.2	Low	Fair
k-ω SST	1.3	Low	Good
RSM	2.0-2.5	Medium	Fair-Poor
DES/DDES	5-20	High	Fair
LES	50-500	Very High	N/A (time-accurate)

Model Constants and Parameters

Standard k-ε Constants

Cμ = 0.09
C1ε = 1.44
C2ε = 1.92
σk = 1.0
σε = 1.3

RNG k-ε Constants

Cμ = 0.0845
C1ε = 1.42
C2ε = 1.68
σk = 0.7179
σε = 0.7179
η0 = 4.38
β = 0.012

Realizable k-ε Constants

C1ε = 1.44
C2 = 1.9
σk = 1.0
σε = 1.2
Cμ = variable (function of strain rate and rotation)

Standard k-ω Constants

α = 5/9
β = 0.075
β* = 0.09
σk = 2.0
σω = 2.0

k-ω SST Constants

k-ω inner:

α1 = 5/9
β1 = 0.075
σk1 = 2.0
σω1 = 2.0

k-ε outer (transformed):

α2 = 0.44
β2 = 0.0828
σk2 = 1.0
σω2 = 1.168

Other:

β* = 0.09
a1 = 0.31 (SST limiter constant)

Spalart-Allmaras Constants

cb1 = 0.1355
cb2 = 0.622
σ = 2/3
κ = 0.41 (von Karman constant)
cw1 = cb1/κ² + (1 + cb2)/σ
cw2 = 0.3
cw3 = 2.0
cv1 = 7.1

Wall Functions vs Wall-Resolved

Standard Wall Functions

Theory:

Based on law of the wall
Assumes equilibrium boundary layer
Logarithmic law: u+ = (1/κ)ln(y+) + B

Requirements:

30 < y+ < 300
Equilibrium turbulent boundary layer
No significant pressure gradients

When to use:

High-Re fully turbulent flows
Simple geometries
Limited computational resources
Steady-state simulations

Limitations:

Inaccurate for adverse pressure gradients
Poor for separation and reattachment
Not suitable for heat transfer predictions
Fails in transitional flows

Scalable Wall Functions

Improvements:

Avoid deterioration for fine meshes
y+ insensitive formulation
Better for y+ < 30

Non-Equilibrium Wall Functions

Improvements:

Account for pressure gradient effects
Improved separation prediction
Better suited for complex flows

When to use:

Flows with pressure gradients
Separation and reattachment
Complex geometries

Enhanced Wall Treatment (EWT)

Characteristics:

Two-layer approach
Blends wall functions (high y+) with low-Re formulation (low y+)
Adaptive based on local y+

When to use:

Variable mesh resolution
Uncertainty in y+ values
Complex geometries with varying resolution

Wall-Resolved (Low-Re)

Requirements:

y+ ≈ 1 (ideally y+ < 1)
10-15+ cells in boundary layer
Growth ratio ≤ 1.2 near wall
Integration to wall (no wall functions)

When to use:

Accurate heat transfer required
Separation prediction critical
Low-Re or transitional flows
Aerodynamic design optimization

Models requiring wall-resolved:

k-ω SST (optimal)
Standard k-ω
Spalart-Allmaras (optimal)
LES

Turbulence Model Selection Decision Tree

START: What is your flow problem?
│
├─ Need time-accurate unsteady structures?
│  │
│  ├─ YES: Go to LES/Hybrid
│  │  │
│  │  ├─ Can afford very fine mesh and long run time?
│  │  │  ├─ YES: LES (wall-resolved or wall-modeled)
│  │  │  └─ NO: DES/DDES (massively separated flows) or SAS
│  │  │
│  │  └─ Is flow primarily attached?
│  │     ├─ YES: URANS (k-ω SST or Realizable k-ε)
│  │     └─ NO: DES/DDES
│  │
│  └─ NO: Continue to RANS selection
│
├─ Flow type?
│  │
│  ├─ External aerodynamics (airfoils, vehicles, aircraft)
│  │  └─ k-ω SST (first choice) or Spalart-Allmaras
│  │     Required: y+ ≈ 1, wall-resolved mesh
│  │
│  ├─ Internal flows (pipes, ducts, channels)
│  │  │
│  │  ├─ Heat transfer important?
│  │  │  ├─ YES: k-ω SST (y+ ≈ 1)
│  │  │  └─ NO: Continue
│  │  │
│  │  ├─ Separation or adverse pressure gradients?
│  │  │  ├─ YES: k-ω SST (y+ ≈ 1) or Realizable k-ε (EWT)
│  │  │  └─ NO: Realizable k-ε (wall functions, y+ = 30-100)
│  │  │
│  │  └─ Simple fully turbulent?
│  │     └─ Standard k-ε (wall functions, y+ = 30-100)
│  │
│  ├─ Free shear flows (jets, wakes, mixing)
│  │  └─ Realizable k-ε or RNG k-ε
│  │
│  ├─ Rotating/swirling flows (turbomachinery, cyclones)
│  │  │
│  │  ├─ Simple rotation?
│  │  │  └─ RNG k-ε or k-ω SST
│  │  │
│  │  └─ Complex 3D rotation with strong curvature?
│  │     └─ RSM (if resources available) or RNG k-ε
│  │
│  └─ Separated flows (backward step, airfoil stall)
│     │
│     ├─ Mild-moderate separation?
│     │  └─ k-ω SST (y+ ≈ 1)
│     │
│     └─ Massive separation?
│        └─ DES/DDES or LES (if affordable)
│
├─ Can you achieve y+ ≈ 1 near walls?
│  │
│  ├─ YES: k-ω SST, Spalart-Allmaras, or Low-Re k-ε
│  │
│  └─ NO: Must use wall functions
│     └─ Realizable k-ε or RNG k-ε (with EWT if possible)
│
└─ Special considerations:
   │
   ├─ Transitional flows (low Re)? → k-ω SST + transition model
   ├─ Compressible/high-speed? → k-ω SST or Spalart-Allmaras
   ├─ Buoyancy-driven? → Realizable k-ε or k-ω SST with buoyancy terms
   ├─ Multiphase flows? → Realizable k-ε or k-ω SST
   └─ Limited resources? → Standard k-ε or Spalart-Allmaras

Quick Selection Guide by Application

Aerospace

Model: k-ω SST or Spalart-Allmaras y+: ≈ 1 Rationale: Accurate prediction of boundary layers, separation, and pressure distribution

Automotive (External)

Model: k-ω SST y+: ≈ 1 Rationale: Separation prediction, drag/lift accuracy

HVAC / Building Ventilation

Model: Realizable k-ε with wall functions y+: 30-100 Rationale: Large domains, computational efficiency, adequate accuracy

Turbomachinery

Model: k-ω SST y+: 1-2 Rationale: Adverse pressure gradients, rotation, heat transfer

Combustion

Model: Realizable k-ε or LES y+: Depends (wall functions for RANS, y+ < 1 for LES) Rationale: Mixing, turbulence-chemistry interaction

Heat Exchangers

Model: k-ω SST or Realizable k-ε with EWT y+: < 5 or wall-resolved Rationale: Heat transfer accuracy critical

Mixing / Chemical Reactors

Model: Realizable k-ε or RSM y+: 30-100 Rationale: Capturing mixing patterns, turbulence anisotropy

Hydraulics (Dams, Spillways)

Model: Realizable k-ε or k-ω SST y+: Variable Rationale: Free surface flows, separation, aeration

Environmental (Atmospheric flows)

Model: Standard k-ε or Realizable k-ε y+: Wall functions Rationale: Large scale, computational cost, atmospheric boundary layer

Best Practices

General Guidelines

Start simple: Begin with simpler models (k-ε, k-ω SST) before trying complex models
Validate mesh: Ensure y+ values are appropriate for chosen model
Check mesh quality: Turbulence models are sensitive to mesh quality
Monitor residuals: Turbulence equations often converge slower than momentum
Use appropriate boundary conditions: Turbulent intensity and length scale matter
Verify sensitivity: Test mesh independence and model sensitivity

Boundary Conditions

Inlet:

Turbulent intensity: I = 0.16 Re^(-1/8) for fully developed pipe flow
Low turbulence: I = 0.1% - 1%
Medium turbulence: I = 1% - 5%
High turbulence: I = 5% - 20%
Turbulent length scale: l ≈ 0.07 × characteristic length

Wall:

No-slip condition
Wall functions or wall-resolved (model dependent)
Roughness can be specified (equivalent sand-grain roughness)

Outlet:

Zero gradient (outflow)
Fixed pressure

Convergence Tips

Initialize properly: Use potential flow or previous solution
Under-relax initially: Start with URF = 0.3-0.5 for turbulence equations
Gradually increase: Increase URF as solution stabilizes
Coupled solvers: Often help with k-ω models
Monitor flow features: Check separation, reattachment, vortex shedding
Residuals alone insufficient: Verify force/flux convergence

Common Pitfalls

Incorrect y+: Most common error; check and adjust mesh
Poor mesh quality: High skewness, aspect ratio issues
Inadequate refinement: In regions of high gradients
Wrong model for application: Using k-ε for separated flows
Freestream sensitivity: k-ω without SST correction
Ignoring validation: Always compare with experiments or benchmarks

Summary Table: RANS Model Comparison

Model	Equations	y+ Requirement	Best For	Avoid For	Computational Cost
Standard k-ε	2	30-300	Simple internal flows, fully turbulent	Separation, low-Re, adverse pressure gradients	Low
RNG k-ε	2	30-300 (or EWT)	Swirl, rotation, moderate separation	Simple flows (overkill)	Low-Medium
Realizable k-ε	2	30-300 (or EWT)	Complex flows, jets, separation, general purpose	Critical aerodynamics	Low-Medium
Standard k-ω	2	≈ 1	Low-Re, transitional, near-wall	Freestream flows (sensitive to ω∞)	Medium
k-ω SST	2	≈ 1	Aerodynamics, separation, adverse pressure gradients	Simple internal flows (expensive)	Medium
Spalart-Allmaras	1	≈ 1	Aerospace, external aerodynamics, mild separation	Internal flows, free shear, complex physics	Low
RSM	7	≈ 1 or 30-300	Anisotropic turbulence, strong swirl, complex 3D	Simple flows, limited resources	High

References

See reference.md for detailed equations, validation cases, and academic references.

turbulence-models-db

More from this repository

Turbulence Models Database

Overview of Turbulence Modeling

Modeling Approaches Hierarchy

RANS Turbulence Models

k-ε Models (k-epsilon)

Standard k-ε

RNG k-ε

Realizable k-ε

k-ω Models (k-omega)

Standard k-ω (Wilcox)

k-ω SST (Shear Stress Transport)

Spalart-Allmaras

Reynolds Stress Models (RSM)

Large Eddy Simulation (LES)

Overview

Subgrid-Scale Models

Smagorinsky-Lilly

Dynamic Smagorinsky

WALE (Wall-Adapting Local Eddy-viscosity)

Kinetic Energy Subgrid-Scale

Applications of LES

Hybrid RANS-LES Methods

DES (Detached Eddy Simulation)

DDES (Delayed DES)

SDES (Shielded DES)

SAS (Scale-Adaptive Simulation)

Model Selection Criteria

Flow Type Classification

Internal Flows

External Flows

Free Shear Flows

Separated Flows

Rotating/Swirling Flows

Reynolds Number Considerations

Mesh Requirements and y+ Values

Wall Functions Approach

Wall-Resolved Approach

Enhanced Wall Treatment

y+ Guidelines by Application

Computational Cost Comparison

Model Constants and Parameters

Standard k-ε Constants

RNG k-ε Constants

Realizable k-ε Constants

Standard k-ω Constants

k-ω SST Constants

Spalart-Allmaras Constants

Wall Functions vs Wall-Resolved

Standard Wall Functions

Scalable Wall Functions

Non-Equilibrium Wall Functions

Enhanced Wall Treatment (EWT)

Wall-Resolved (Low-Re)

Turbulence Model Selection Decision Tree

Quick Selection Guide by Application

Aerospace

Automotive (External)

HVAC / Building Ventilation

Turbomachinery

Combustion

Heat Exchangers

Mixing / Chemical Reactors

Hydraulics (Dams, Spillways)

Environmental (Atmospheric flows)

Best Practices

General Guidelines

Boundary Conditions

Convergence Tips

Common Pitfalls

Summary Table: RANS Model Comparison

References

Turbulence Models Database

Overview of Turbulence Modeling

Modeling Approaches Hierarchy

RANS Turbulence Models

k-ε Models (k-epsilon)

Standard k-ε

RNG k-ε