Two-Phase Flow Patterns
and Flow-Pattern Maps
Mostafa Ghadamyari
M.SC Student, Mechanical Engineering, Tarbiat Modares University
Spring 2014
1
Why study two-phase flows?
Example: Dead water Phenomenon
 1893 Fridtjof Nansen
 Occurs when fresh water rests on
dense salt water
 Much of the energy results in
waves and turbulence of
interface
 Reduce in traveling speed by 80%
 If V>Vcritical Then the phenomenon
disappears
2
Two-phase Flow-Patterns
Flow pattern definition:
 Various gas-liquid interfacial
geometric configurations in two-
phase flow systems.
 The physical mechanisms
controlling two-phase pressure
drops and heat transfer
coefficients are intrinsically related
to the local flow patterns
Vertical tubes Flow-patterns :
3
Increasing Vg
Two-phase Flow-Patterns
Horizontal Tube Flow-patterns :
4
 Stratified : Small Vg & VL
 Increasing both Vg & VL : Wavy
 Increased VL but small Vg : Plug, If
bubbles are small : Dispersed
Bubble
 Plug + Increase Vg : Slug
 Slug + Increase Vg : Annular and
then Mist
Different Conditions,
Different Flows :
Two-phase Flow-Patterns
Horizontal tube videos Vertical tube videos
5
 Ammonia @ 5C
 Horizontal Tube, d=14mm
 Zürcher, Thome, Favrat
 Swiss Federal Institute of
Technology Lausanne
(EPFL).
 Air & Water @ 25C
 Vertical Tube, d=30mm
 Zun and Polutnik
 University of Ljubljana,
Slovenia
Diabatic Two-Phase Flows
Upward Flow Boiling In A Vertical & Horizontal Tube :
6
 Pressure drop & Heat transfer coefficient are related to two-phase Flow Patterns
 Collier, J. G., and Thome, J. R., 1994,Convective Boiling and Condensation
Diabatic Two-Phase Flows
Condensation in Horizontal Tube :
7
 Condensation film forms Annular
flow in the entrance
 As condensation continues, the
vapor velocity falls
 At high flow rates, slug and
bubble flows are eventually
reached
 At low flow rates large magnitude
waves and then stratified flow are
formed.
Palen, J. W., Breber, G., and Taborek, K.,
1979, “Prediction of Flow Regimes
in Horizontal Tube-Side-Condensation,”
Flow Pattern Maps
 To predict local flow patterns, two-phase
flow-pattern maps are used.
 Mostly developed for adiabatic conditions
 First paper published in 1950
 Two categories :
 1. Empirical Flow-Pattern Maps
 The Baker, Hewitt & Roberts, …
 2. Theoretical Flow-Pattern Maps
 Taitel and Dukler, …
8
Flow Pattern Maps
The Baker flow-pattern map for
horizontal gas-liquid cocurrent flow.
9
The Hewitt and Roberts flow-pattern
map for vertical upward gas-liquid
cocurrent flow
Based on observations of cocurrent flow of gaseous and
condensate petroleum products in horizontal pipes.
Flow Pattern Maps
The Theoretical Taitel and Dukler flow-
pattern map for horizontal gas-liquid
cocurrent flow :
The Kattan–Thome–Favrat flow-
pattern map compared to the
Steiner map :
10
Evaluated for R410A at Tsat=5°C in a 13.84 mm
internal diameter tube at different heat fluxes
X : Martinelli parameter
X= [(dP/dZ)L / (dP/dZ)G]^0.5
Summary
 We discussed about:
 Different types of two-phase flow patterns
 Flow patterns in horizontal and vertical tubes
 Flow Pattern maps:
 1. Experimental maps
 Baker, Hewitt & Robert, …
 2. Theoretical maps
 Taitel & Dukler
11
12

Two-Phase Flow Patterns and Flow-Pattern Maps

  • 1.
    Two-Phase Flow Patterns andFlow-Pattern Maps Mostafa Ghadamyari M.SC Student, Mechanical Engineering, Tarbiat Modares University Spring 2014 1
  • 2.
    Why study two-phaseflows? Example: Dead water Phenomenon  1893 Fridtjof Nansen  Occurs when fresh water rests on dense salt water  Much of the energy results in waves and turbulence of interface  Reduce in traveling speed by 80%  If V>Vcritical Then the phenomenon disappears 2
  • 3.
    Two-phase Flow-Patterns Flow patterndefinition:  Various gas-liquid interfacial geometric configurations in two- phase flow systems.  The physical mechanisms controlling two-phase pressure drops and heat transfer coefficients are intrinsically related to the local flow patterns Vertical tubes Flow-patterns : 3 Increasing Vg
  • 4.
    Two-phase Flow-Patterns Horizontal TubeFlow-patterns : 4  Stratified : Small Vg & VL  Increasing both Vg & VL : Wavy  Increased VL but small Vg : Plug, If bubbles are small : Dispersed Bubble  Plug + Increase Vg : Slug  Slug + Increase Vg : Annular and then Mist Different Conditions, Different Flows :
  • 5.
    Two-phase Flow-Patterns Horizontal tubevideos Vertical tube videos 5  Ammonia @ 5C  Horizontal Tube, d=14mm  Zürcher, Thome, Favrat  Swiss Federal Institute of Technology Lausanne (EPFL).  Air & Water @ 25C  Vertical Tube, d=30mm  Zun and Polutnik  University of Ljubljana, Slovenia
  • 6.
    Diabatic Two-Phase Flows UpwardFlow Boiling In A Vertical & Horizontal Tube : 6  Pressure drop & Heat transfer coefficient are related to two-phase Flow Patterns  Collier, J. G., and Thome, J. R., 1994,Convective Boiling and Condensation
  • 7.
    Diabatic Two-Phase Flows Condensationin Horizontal Tube : 7  Condensation film forms Annular flow in the entrance  As condensation continues, the vapor velocity falls  At high flow rates, slug and bubble flows are eventually reached  At low flow rates large magnitude waves and then stratified flow are formed. Palen, J. W., Breber, G., and Taborek, K., 1979, “Prediction of Flow Regimes in Horizontal Tube-Side-Condensation,”
  • 8.
    Flow Pattern Maps To predict local flow patterns, two-phase flow-pattern maps are used.  Mostly developed for adiabatic conditions  First paper published in 1950  Two categories :  1. Empirical Flow-Pattern Maps  The Baker, Hewitt & Roberts, …  2. Theoretical Flow-Pattern Maps  Taitel and Dukler, … 8
  • 9.
    Flow Pattern Maps TheBaker flow-pattern map for horizontal gas-liquid cocurrent flow. 9 The Hewitt and Roberts flow-pattern map for vertical upward gas-liquid cocurrent flow Based on observations of cocurrent flow of gaseous and condensate petroleum products in horizontal pipes.
  • 10.
    Flow Pattern Maps TheTheoretical Taitel and Dukler flow- pattern map for horizontal gas-liquid cocurrent flow : The Kattan–Thome–Favrat flow- pattern map compared to the Steiner map : 10 Evaluated for R410A at Tsat=5°C in a 13.84 mm internal diameter tube at different heat fluxes X : Martinelli parameter X= [(dP/dZ)L / (dP/dZ)G]^0.5
  • 11.
    Summary  We discussedabout:  Different types of two-phase flow patterns  Flow patterns in horizontal and vertical tubes  Flow Pattern maps:  1. Experimental maps  Baker, Hewitt & Robert, …  2. Theoretical maps  Taitel & Dukler 11
  • 12.