new plate baffle water flow. quick simulation use triangular prism as rough estimate of a vane...

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New Plate Baffle Water Flow

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Page 1: New Plate Baffle Water Flow. Quick Simulation Use triangular prism as rough estimate of a vane Uniform heat flux on each surface –600 kWm -2 on end face

New Plate Baffle Water Flow

Page 2: New Plate Baffle Water Flow. Quick Simulation Use triangular prism as rough estimate of a vane Uniform heat flux on each surface –600 kWm -2 on end face

Quick Simulation• Use triangular prism as rough estimate of a vane

• Uniform heat flux on each surface– 600 kWm-2 on end face (highest flux at cutback…

average would be much less!)– 20 kWm-2 on side faces– Symmetry at other end, stagnant air convection on top

surface

• See what temperature copper gets to

• (Next, use better vane shape and heat flux)

Page 3: New Plate Baffle Water Flow. Quick Simulation Use triangular prism as rough estimate of a vane Uniform heat flux on each surface –600 kWm -2 on end face

Flow Estimates

pcm

PT

2504.1

7513.1

1419.5H

av

D

vLp

H

u

D

kNHTC

Total power, P, to be removed from 355mm long prism ≈ 2 kW

Water mass flow rate, , per pipe = 0.157 kgs-1 (assuming flow speed = 2 ms-1 = 9.42 L min-1)

Estimated temperature rise, ΔT, of cooling water ≈ 3 °CPipe length, L, within copper = 2.1 mAverage water flow rate vav = 2 ms-1

Pipe diameter, DH = 10 mmEstimated pressure drop, Δp = 0.12 Bar

m

Nusselt number, Nu, of water flow = 144.2Thermal conductivity of water, k = 0.6 Wm-1K-1

Estimated heat transfer coefficient = 8650 Wm-2K-1

Page 4: New Plate Baffle Water Flow. Quick Simulation Use triangular prism as rough estimate of a vane Uniform heat flux on each surface –600 kWm -2 on end face

Very crude approximation of vane shape and input heat flux, but overall temperature distribution is comparable to previous, more accurate simulations (small image above)

Page 5: New Plate Baffle Water Flow. Quick Simulation Use triangular prism as rough estimate of a vane Uniform heat flux on each surface –600 kWm -2 on end face

Average Outlet Water Temperature = 18 °C

Inlet Water Temperature = 15 °C

Racetrack path of water flow repeatedly redistributes heat from primary heat input region on left to cooler region on right.

Water absorbs a lot of heat

Water becomes cooler again

Page 6: New Plate Baffle Water Flow. Quick Simulation Use triangular prism as rough estimate of a vane Uniform heat flux on each surface –600 kWm -2 on end face

Average HTC = 9000 Wm-2K-1

Higher HTCs on thinner channels where water flow is faster

Page 7: New Plate Baffle Water Flow. Quick Simulation Use triangular prism as rough estimate of a vane Uniform heat flux on each surface –600 kWm -2 on end face

Sharp transitions between layers increase the water pressure significantly compared to estimate for smooth cooling channel

Page 8: New Plate Baffle Water Flow. Quick Simulation Use triangular prism as rough estimate of a vane Uniform heat flux on each surface –600 kWm -2 on end face

Comparison of ResultsProperty Hand estimate ANSYS CFD Result

Mass flow rate 0.157 kgs-1 (9.42 Lmin-1)

0.1545 kgs-1 (9.27 Lmin-1)

Average water flow 2 ms-1 1.914 ms-1

Maximum water flow 5 ms-1 (desired upper limit)

4.227 ms-1

Total Pressure 0.12 Bar 0.375 Bar

Average HTC 8650 Wm-2K-1 9000 Wm-2K-1

Water temperature rise

3 °C 3 °C

Simulation matches back-of-the-envelope calculations (again… well done ANSYS!)

Copper temperature similar to previous simulations with different flow Good

To do now: try a more accurate model and put in a squirt nozzle