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CDT WP2 5th technical meeting Mol 05/2011 Vincent Moreau

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Presentation on theme: "CDT WP2 5th technical meeting Mol 05/2011 Vincent Moreau"— Presentation transcript:

1 CDT WP2 5th technical meeting Mol 05/2011 Vincent Moreau
FASTEF Primary pump/HX assembly update and preliminary tube rupture simulations CDT meeting 01/2011 Brussel CDT WP2 5th technical meeting Mol 05/2011 Vincent Moreau

2 Summary Design update Control Simulation Single bubble leak (1)
Simulation Results Simulation/Design update Single bubble leak (2) Pump pre-design Merging for large gas leak What next CDT meeting 01/2011 Brussel

3 Design update Addition of a chimney Enlarged pump casing
The initial and updated CAD design have been provided by Marco Ottolini Addition of a chimney Enlarged pump casing Larger open volume below the HX CDT meeting 01/2011 Brussel The update has been the occasion to clean/simplify the flow diverter structure.

4 Design update Previous proposal First update
CDT meeting 01/2011 Brussel Previous proposal First update

5 Simulation: numerical setting
Default stationary setting Inlet mass flow rate: 815 kg/s (total: 815x8=6520 kg/s, slightly too low, objective 7500 kg/s), LBE density: kg/m3 (573K, HLM Handbook) LBE viscosity: 1.84e-3 Pa.s Realizable k-e turbulence model Two-Layer All y+ Wall treatment Passive scalar for residence time evaluation Passive scalar source term (value=density) except in the HX CDT meeting 01/2011 Brussel

6 Simulation Results CDT meeting 01/2011 Brussel Reasonable flow regulation with the radial separators obtained at the second trial

7 Simulation Results CDT meeting 01/2011 Brussel Bubble size issue: inlet velocity should be preserved Also technical problems: forced to rebuild the geometry from scratch

8 Geometry update Equivalent inlet section Counter tube re-profiling
CDT meeting 01/2011 Brussel

9 Simulation Results Velocity magnitude and residence time
CDT meeting 01/2011 Brussel

10 Simulation Results Bubble injection from the HX tubes bottom
3 out of 50 2mm bubbles flow down to the propeller CDT meeting 01/2011 Brussel

11 Simulation Results Bubble injection from the HX tubes bottom
1 out of 50 2mm bubbles flow down to the propeller Critical zone located CDT meeting 01/2011 Brussel

12 Include pump design Need to include, even roughly, features of the pump current design (by Sebastien Mortier) Upper diaphragm level Almost sealed CDT meeting 01/2011 Brussel Windows

13 Large gas leak Need to enlarge the simulation domain
Gas insertion forces LBE out There are 4 possible outlets: 2 HXs, chimney and pump outlet. Reaction of the 4 outlets also depend on the “far field” An “almost” equivalent of the entire loop had to be built CDT meeting 01/2011 Brussel

14 Large gas leak Enlarged simulation domain: Two half-HX
Large inner vessel volume Core mockup (hydraulic resistance) Large outer vessel volume Remote handling volume Volumetric force for the pump CDT meeting 01/2011 Brussel

15 Large gas leak Mesh 2MCells Size 2-10cm

16 Large gas leak Time needed to create the surface shift (days)

17 Large gas leak Long transient to get a reasonable initial condition (25s) LBE mass flow at beginning event: 1350 kg/s (should be 1750 kg/s)

18 Large gas leak Two different locations for the gas source Case 3
Case 1 and 2

19 Large gas leak Case 1: gas source 50 dm3/s in 1s exp ramp
Source location: tube basis, close to the inner wall Physical time 4.5 s Shown: iso-surface 0.5 of volumetric fraction

20 Large gas leak Case 1, 50 dm3/s

21 Large gas leak Case 2: gas source 250 dm3/s in 1s exp ramp
Source location: tube basis, close to the inner wall Physical time s Shown: iso-surface 0.5 of volumetric fraction

22 Large gas leak Case 2, 250 dm3/s

23 Large gas leak Case 3: gas source 50 dm3/s in 1s exp ramp
Source location: 12 cm over tube basis, close to the outer shell Physical time 4.1 s Shown: iso-surface 0.5 of volumetric fraction

24 Large gas leak Case 3, 50 dm3/s

25 Large gas leak Case 2 (250 l/s) Initial and final VM field

26 Large gas leak Case 2 Pump mass flow history

27 Large gas leak Case 2 Gas flow rate

28 Large gas leak What to do next:
Increase the LBE flow rate to 1750 kg/s Test higher gas rate ? Report ?

29 Thank you for your attention
End Thank you for your attention CDT meeting 01/2011 Brussel


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