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DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 1
Source: The Internet
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 2
Confluence research @ Ugent
Laurent Schindfessel
Extreme discharge ratios
Large-eddy simulation
Stéphan Creëlle
Mixing & headloss prediction
Experiments
Promotor: Tom De Mulder
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
Hydraulics laboratory
pag. 3Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 4
h3
Q1
Q2
h1
h2
Q1+Q2
?
?
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 5
h1=h2
h1/h2 [-]
q [-]
Generally
accepted
Equation 1?
Equation 2?
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 6
Multiple solutions reported in
literature
Equality model Energy approach Momentum approach
-simple
-easy to implement
h1=h2=h3
-simple
-errors up to
50% h3
E1+E2+ ΔE=E3
-empirical loss coeff.
-combines easily
with other energy
loss formulations
-limited information
M1,x+M2,x+ SF=M3,x
-allows for best calculation
of different terms
-additional computational
effort
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 7
M1+M2 cos θ − M3=P3 − P1 − P2cos θ − PWALLS sin θ
3
1
M1,x+M2,x-M3,x =-SF
𝑀3, 𝑃3
𝑀2, 𝑃2
𝑀2, 𝑃2
𝑃 𝑊𝐴𝐿𝐿𝑆
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 8
Can be expressed with the variables of the problem:
𝑃 =
𝜌ℎ2
𝑊
2
?
𝑀 =
𝜌𝑄2
ℎ𝑊
M1+M2 cos θ − M3=P3 − P1 − P2cos θ − PWALLS sin θ
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 9
Taylor(1944)
ℎ 𝑇𝐼𝑊 = ℎ 𝑇𝑂𝑊 = ℎ2
Can be expressed with the variables of the problem:
𝑀 =
𝜌𝑄2
ℎ𝑊
𝑃 =
𝜌ℎ2
𝑊
2
?
M1+M2 cos θ − M3=P3 − P1 − P2cos θ − PWALLS sin θ
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 10
Taylor(1944)
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 11
Taylor(1944)
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 12
Webber & Greated(1966)
Pressure difference over the
channel walls due to
contraction to the
downstream corner
Change in physical inflow
angle α in the TCS
Cause of deviations?
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 13
PWALLS
𝑴 𝟐
=
𝟏 − 𝒒
𝒒
Ramamurthy(1988)
Hager(1998)
𝑴 𝟐
𝒕𝒂𝒏 𝜶
= PWALLS
α=
8
9
θ
α=acos [0.149 + 0.914 (1 − 𝑞)]
Hsu(1998)(for θ=90°)
Angle Wall pressure
difference
PWALLS sin θ
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 14
0,95
1
1,05
1,1
1,15
1,2
1,25
1,3
1,35
1,4
0 0,2 0,4 0,6 0,8 1
h1/h3[-]
q[-]
Hsu (1998) 30°
Hager (1989) 30°
Hsu (1998) 60°
Hager (1989) 60°
Hsu (1998) 90°
Hager (1989) 90°
equality
Fr3=0.55
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 15
0,95
1,05
1,15
1,25
1,35
1,45
1,55
1,65
1,75
0 0,1 0,2 0,3 0,4 0,5 0,6 0,7 0,8 0,9 1
h1/h3[-]
Fr3
0.1
0.25
0.5
q [-]
0.75
0.9
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
pag. 16
Conclusions:
-Head losses near confluences become more significant when:
-Froude numbers increase
-The confluence angle increases
-For low angles and Froude numbers, the equality model can
suffice. For the other cases, an energy or momentum
approach should be incorporated.
-The momentum conservation approach delivers the most applicable
results, but for high angles the tributary momentum contribution should be
formulated accurately.
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 17
Work in progress:
-Description of the tributary momentum contribution, based on
theoretical description of the velocity profiles in the tributary
branch, in order to obtain more reliable results, and to
eliminate the need for empirical expressions for the tributary
momentum contribution or inflow angle
-Experimental measurements of the flow behaviour of the flow
in the tributary branch in the approach of the confluence area.
-Description of the mixing, momentum exchange and
uniformization process in and downstream of the confluence,
based on experimental measurements of the surface
velocities.
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 18
Thanks for your attention!
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 19
References:
Taylor, E. H. (1944). Flow characteristics at rectangular open-channel
junctions. Trans. ASCE(107), 893–912.
Webber, N. B., & Greated, C. (1966). An investigation of flow behaviour at
the junction of rectangular channels. Paper presented at the ICE
Proceedings.
Hsu, C.-C., Wu, F.-S., & Lee, W.-J. (1998). Flow at 90 equal-width open-
channel junction. Journal of Hydraulic Engineering, 124(2), 186-191.
Hager, W. (1989). Transitional Flow in Channel Junctions. Journal of
Hydraulic Engineering, 115(2), 243-259. doi: doi:10.1061/(ASCE)0733-
9429(1989)115:2(243)
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
DEPT. OF CIVIL ENGINEERING
Hydraulics laboratory
pag. 20
Assumptions:
1) All channels have a rectangular shaped cross-section with width W,
2) The beds of the main channel and the tributary are concordant, fixed and
horizontal,
3) In the cross-sections 1, 2 and 3, the flow is uniform and the water surface is
horizontal,
4) Friction losses due to the banks and the beds can be neglected,
5) Pressure distributions are hydrostatic in the sections considered and along the
walls
Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder
Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp

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Stephan the importance of confluences in hydraulic network models of rivers

  • 1. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 1 Source: The Internet Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 2. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 2 Confluence research @ Ugent Laurent Schindfessel Extreme discharge ratios Large-eddy simulation Stéphan Creëlle Mixing & headloss prediction Experiments Promotor: Tom De Mulder Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 3. Hydraulics laboratory pag. 3Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 4. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 4 h3 Q1 Q2 h1 h2 Q1+Q2 ? ? Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 5. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 5 h1=h2 h1/h2 [-] q [-] Generally accepted Equation 1? Equation 2? Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 6. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 6 Multiple solutions reported in literature Equality model Energy approach Momentum approach -simple -easy to implement h1=h2=h3 -simple -errors up to 50% h3 E1+E2+ ΔE=E3 -empirical loss coeff. -combines easily with other energy loss formulations -limited information M1,x+M2,x+ SF=M3,x -allows for best calculation of different terms -additional computational effort Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 7. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 7 M1+M2 cos θ − M3=P3 − P1 − P2cos θ − PWALLS sin θ 3 1 M1,x+M2,x-M3,x =-SF 𝑀3, 𝑃3 𝑀2, 𝑃2 𝑀2, 𝑃2 𝑃 𝑊𝐴𝐿𝐿𝑆 Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 8. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 8 Can be expressed with the variables of the problem: 𝑃 = 𝜌ℎ2 𝑊 2 ? 𝑀 = 𝜌𝑄2 ℎ𝑊 M1+M2 cos θ − M3=P3 − P1 − P2cos θ − PWALLS sin θ Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 9. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 9 Taylor(1944) ℎ 𝑇𝐼𝑊 = ℎ 𝑇𝑂𝑊 = ℎ2 Can be expressed with the variables of the problem: 𝑀 = 𝜌𝑄2 ℎ𝑊 𝑃 = 𝜌ℎ2 𝑊 2 ? M1+M2 cos θ − M3=P3 − P1 − P2cos θ − PWALLS sin θ Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 10. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 10 Taylor(1944) Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 11. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 11 Taylor(1944) Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 12. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 12 Webber & Greated(1966) Pressure difference over the channel walls due to contraction to the downstream corner Change in physical inflow angle α in the TCS Cause of deviations? Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 13. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 13 PWALLS 𝑴 𝟐 = 𝟏 − 𝒒 𝒒 Ramamurthy(1988) Hager(1998) 𝑴 𝟐 𝒕𝒂𝒏 𝜶 = PWALLS α= 8 9 θ α=acos [0.149 + 0.914 (1 − 𝑞)] Hsu(1998)(for θ=90°) Angle Wall pressure difference PWALLS sin θ Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 14. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 14 0,95 1 1,05 1,1 1,15 1,2 1,25 1,3 1,35 1,4 0 0,2 0,4 0,6 0,8 1 h1/h3[-] q[-] Hsu (1998) 30° Hager (1989) 30° Hsu (1998) 60° Hager (1989) 60° Hsu (1998) 90° Hager (1989) 90° equality Fr3=0.55 Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 15. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 15 0,95 1,05 1,15 1,25 1,35 1,45 1,55 1,65 1,75 0 0,1 0,2 0,3 0,4 0,5 0,6 0,7 0,8 0,9 1 h1/h3[-] Fr3 0.1 0.25 0.5 q [-] 0.75 0.9 Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 16. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp pag. 16 Conclusions: -Head losses near confluences become more significant when: -Froude numbers increase -The confluence angle increases -For low angles and Froude numbers, the equality model can suffice. For the other cases, an energy or momentum approach should be incorporated. -The momentum conservation approach delivers the most applicable results, but for high angles the tributary momentum contribution should be formulated accurately.
  • 17. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 17 Work in progress: -Description of the tributary momentum contribution, based on theoretical description of the velocity profiles in the tributary branch, in order to obtain more reliable results, and to eliminate the need for empirical expressions for the tributary momentum contribution or inflow angle -Experimental measurements of the flow behaviour of the flow in the tributary branch in the approach of the confluence area. -Description of the mixing, momentum exchange and uniformization process in and downstream of the confluence, based on experimental measurements of the surface velocities. Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 18. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 18 Thanks for your attention! Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 19. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 19 References: Taylor, E. H. (1944). Flow characteristics at rectangular open-channel junctions. Trans. ASCE(107), 893–912. Webber, N. B., & Greated, C. (1966). An investigation of flow behaviour at the junction of rectangular channels. Paper presented at the ICE Proceedings. Hsu, C.-C., Wu, F.-S., & Lee, W.-J. (1998). Flow at 90 equal-width open- channel junction. Journal of Hydraulic Engineering, 124(2), 186-191. Hager, W. (1989). Transitional Flow in Channel Junctions. Journal of Hydraulic Engineering, 115(2), 243-259. doi: doi:10.1061/(ASCE)0733- 9429(1989)115:2(243) Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp
  • 20. DEPT. OF CIVIL ENGINEERING Hydraulics laboratory pag. 20 Assumptions: 1) All channels have a rectangular shaped cross-section with width W, 2) The beds of the main channel and the tributary are concordant, fixed and horizontal, 3) In the cross-sections 1, 2 and 3, the flow is uniform and the water surface is horizontal, 4) Friction losses due to the banks and the beds can be neglected, 5) Pressure distributions are hydrostatic in the sections considered and along the walls Stéphan Creëlle- Stephan.Creelle@ugent.be –Tom De Mulder Belgian Hydraulics Day - 5/10/2015 – FHR Antwerp