15
Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in Milan

Turbulent Bounded Flows for Oil & Gas Industry CFD Module · Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in

  • Upload
    others

  • View
    2

  • Download
    0

Embed Size (px)

Citation preview

Page 1: Turbulent Bounded Flows for Oil & Gas Industry CFD Module · Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in

Turbulent Bounded Flows for Oil

& Gas Industry

CFD Module

Excerpt from the Proceedings of the 2012 COMSOL Conference in Milan

Page 2: Turbulent Bounded Flows for Oil & Gas Industry CFD Module · Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in

Introduction

Reynolds’ Experiment:

Transition: Re=2.200

Eddies

Turbulent Vsicosity

Bounded Flows: Streamlines

Head Loss

Time of Residence

Re from 200 to 600.000

Pressure Equipment Directive

Organisation Internationale de Métrologie Légale

Customer -oriented

Page 3: Turbulent Bounded Flows for Oil & Gas Industry CFD Module · Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in

CFD with COMSOL

Modeling means approximation:

Spalart - Almaras

k-ε

k-ω (Bounded Flows)

Almost automatic meshing:

Size –Bulk

Size – Boundary

Manual Boundary Layer Mesh, 1st Layer Thickness

Solvers:

Iterative

Direct - PARDISO

Page 4: Turbulent Bounded Flows for Oil & Gas Industry CFD Module · Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in

Air Separator DV CAD & Mesh

Page 5: Turbulent Bounded Flows for Oil & Gas Industry CFD Module · Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in

DV – Results (1)

Check Dimensionless Wall

Distance for consistency

Data can be extracted through

3D/2D plot and specific

operations (model couplings)

Page 6: Turbulent Bounded Flows for Oil & Gas Industry CFD Module · Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in

DV – Results (2)

Streamlines highlight vortex formation

Upper and lower vertices of vortex

coincide with local maxima for

dimensional wall distance

Page 7: Turbulent Bounded Flows for Oil & Gas Industry CFD Module · Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in

DV – Results (3)

0

0.02

0.04

0.06

0.08

0.1

0.12

0.14

0 500 1000 1500 2000 2500 3000

Head

Lo

ss (

bar)

Flow Rate (L/min)

Series1

JetA1

Fuel

Pressure Drop as a Function of Flow Rate

Page 8: Turbulent Bounded Flows for Oil & Gas Industry CFD Module · Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in

DV – Results (4)

Page 9: Turbulent Bounded Flows for Oil & Gas Industry CFD Module · Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in

Flow Meter BM - Model

Irregular Geometry: Aspect Ratio ≈1.500

Moving Walls Functions: Thickness 1° Layer B.L.M.

Dimensionless Wall Distance

Dimensional Wall Distance

D.O.F. up to 1.7e6

Transition???

Page 10: Turbulent Bounded Flows for Oil & Gas Industry CFD Module · Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in

Flow Meter BM Validation

Page 11: Turbulent Bounded Flows for Oil & Gas Industry CFD Module · Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in

New BM

Small Changes in Geometry:

Reduce re-circulation

Avoid negative effects on head loss

Influence of Geometry

Page 12: Turbulent Bounded Flows for Oil & Gas Industry CFD Module · Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in

New BM

Dimenionless Wall Distance

must always equal 11.06

Dimensional Wall

Distance must always be

less than local

characteristic lengths

Consistency

Page 13: Turbulent Bounded Flows for Oil & Gas Industry CFD Module · Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in

New BM

Good: one model then another

Bad: same file (300MB on average)

Build different geometries and couple them together

Coupling

Page 14: Turbulent Bounded Flows for Oil & Gas Industry CFD Module · Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in

Check for Consistency

Page 15: Turbulent Bounded Flows for Oil & Gas Industry CFD Module · Turbulent Bounded Flows for Oil & Gas Industry CFD Module Excerpt from the Proceedings of the 2012 COMSOL Conference in

Conclusion

Sweet: CAD – parametric design, import

Almost Automatic Meshing

Almost Automatic Solver

Bitter: Impinging Flows

Iterative Control for Consistency

Monolithic Files

Good & Bad