e. da riva/m. gomez marzoa1 wg4 meeting - 18th july 2012 ultra-light carbon fiber structures: first...

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E. Da Riva/M. Gomez Marzoa 1 WG4 Meeting - 18th July 2012 Ultra-light carbon fiber structures: first test campaign Enrico DA RIVA (EN-CV-PJ) Manuel GOMEZ MARZOA (EN-CV-PJ) 18 th July 2012

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E. Da Riva/M. Gomez Marzoa 1WG4 Meeting - 18th July 2012

Ultra-light carbon fiber structures: first

test campaign

Enrico DA RIVA (EN-CV-PJ)

Manuel GOMEZ MARZOA (EN-CV-PJ)

18th July 2012

E. Da Riva/M. Gomez Marzoa 2WG4 Meeting - 18th July 2012

Outline Thermal tests done over the structure already tested by the Bari team.

Pipe OD [mm] 1.5

Pipe thickness [mm] 0.035

Pipe ID [mm] 1.43

CF strip thickness tcs [mm] 0.07

CF tangential coverage β [deg] 270

Pitch p+w [mm] 7.5

Fiber width w [mm] 1.5

Separation central line fibers p [mm] 6

Angle fibers with pipe axis α [deg] 23

E. Da Riva/M. Gomez Marzoa 3WG4 Meeting - 18th July 2012

Setup description

E. Da Riva/M. Gomez Marzoa 4WG4 Meeting - 18th July 2012

Setup procedure1. Assemble the circuit

2. Connect the sensors to the Data Acquisition System through ELMB cards

Existing channel configuration used: no need to recalibrate ELMB

3. Build up the PVSS panel

4. Connect the circuit bypassing prototype: flush water

Check the reading of the sensors

5. Connect prototype and flush water

6. Start measurements

Heater emissivity:

ε=0.86 (for

thermo camera)

Insulation placed

over the PTs and

connectors

E. Da Riva/M. Gomez Marzoa 5WG4 Meeting - 18th July 2012

Results Six cases done, corresponding to the experiments done in Bari

An absolute power equal to 11.7 W applied to heater (see Bari presentation):

Rheater = 27.2 Ω

P = I2 R; I= (11.7/27.2)0.5 = 0.65 A

V = I R = 0.65*27.2 = 17.7 V

From case number 3 onwards, insulation was put over the aluminum connectors

and the PTs at the piping

Temperature of the heater remains stable even when increasing the flow rate

N m [kg h-1] P [W] Tin [oC] Tout [oC] T1 [oC] T2 [oC] T3 [oC] T4 [oC] pin [bar] pout [bar] ΔP [bar]

1 7.6 11.7 15.3 16.21 29.42 29.231 29.004 27.655 2.74 2.47 0.27

2 8.124 11.7 15.14 16 29.083 29.031 28.673 27.372 2.76 2.47 0.29

3 8.224 11.7 14.8 15.78 29.5 29 28.8 27.5 2.72 2.41 0.31

4 11.41 11.7 14.66 16.44 28.4 27.9 27.8 27.1 2.98 2.41 0.57

5 13.7 11.7 14.5 15.2 28 27.4 27.2 26.7 3.23 2.42 0.81

6 15.8 11.7 14.62 15.1 27.9 27.34 27.13 26.7 3.47 2.4 1.07

E. Da Riva/M. Gomez Marzoa 6WG4 Meeting - 18th July 2012

Results – Thermal picturesInlet/outletHotspot outside

the stave cooling area

7.60 lpm

8.12 lpm

8.22 lpm

11.41 lpm

13.70 lpm

15.8 lpm

Silicon

E. Da Riva/M. Gomez Marzoa 7WG4 Meeting - 18th July 2012

Results – Thermal pictures (Bari)

E. Da Riva/M. Gomez Marzoa 8WG4 Meeting - 18th July 2012

Results – Thermal pictures

8.22 lpm

Silicon

Hotspots on the heater:

Points Temperature [°C]

a 34.17

b 31.53

c 31.38

d 31.38

e 30.78

f 30.03

g 30.03

h 29.88

Hottest point is at the heater end, outside the

cooled area (silicon)

Heater is supposed to be cooled there by the

water at the pipe turn and the stave by thermal

conduction along the heater.

Inlet/outlet

E. Da Riva/M. Gomez Marzoa 9WG4 Meeting - 18th July 2012

Results – Thermal pictures

8.22 lpm

Silicon

Temperature along three lines at the stave:

Inlet/outlet

T line 1

T line 2

T line 3

E. Da Riva/M. Gomez Marzoa 10WG4 Meeting - 18th July 2012

Results

The first test (@7.6 lpm) can be

neglected, the results do not

follow the trend of the rest.

Noticeable decrease of silicon

maximum temperature when

transition to turbulent flow

happens (~ 12 lpm).

E. Da Riva/M. Gomez Marzoa 11WG4 Meeting - 18th July 2012

ResultsΔT wall-water

m [l/h] V [m/s] ReΔp exp [bar]

Δp duct [bar]

HTC (lam)

HTC (Gniel) LAM TURB

7.60 1.31 1649 0.27 0.12 1646 3596 3.2 1.458.12 1.40 1762 0.29 0.12 1646 4162 3.2 1.258.22 1.42 1784 0.31 0.13 1646 4268 3.2 1.22

11.41 1.97 2475 0.57 0.17 1646 7465 3.2 0.7013.70 2.36 2972 0.81 0.45 1646 9594 3.2 0.5415.80 2.73 3427 1.05 0.56 1646 11462 3.2 0.45

Difference in pressure drop with the expected theoretical values is due to the

connectors, piping, etc. These losses can be considered as k*1/2*ρ*v2, where k is

a constant dependent on the setting and can be calculated.

ΔT wall-water: establishes the margin of improvement by using a better

cooling system for this setup:

HTC wall-fluid [W m-2 K-1] Tmax Silicon [oC]

1646 43.02

5000 39.25

10000 38.22

E. Da Riva/M. Gomez Marzoa 12WG4 Meeting - 18th July 2012

Outcome1. Experiences can be run fast and reliably.

2. Uncertainty: big

Sensors (PTs, NTCs, p sensors, flow meter).

Thermo camera: -/+4 oC below 100 oC

Systematic: depends on the setup (assembly of sensors, NTCs over heater).

Thermo camera shooting point: not fixed this time (reflections can appear).

Results qualitatively significant

3. Standardized setup necessary:

Stave support for quick replacement.

Tripod for thermo camera.

NTCs glued to the heater to enhance local contact.

4. Evaporative cooling system little improves thermal performance, but could ensure

better T distribution.

5. Water tests can be repeated using the same absolute power as in the Bari

experiences (13.7 W corresponding to 0.71 A current)

E. Da Riva/M. Gomez Marzoa 13WG4 Meeting - 18th July 2012

Ultra-light carbon fiber structures: first

test campaign

Enrico DA RIVA (EN-CV-PJ)

Manuel GOMEZ MARZOA (EN-CV-PJ)

18th July 2012