calorimeter analysis tasks, july 2014 revision b january 22, 2015

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Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

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Page 1: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

Calorimeter Analysis Tasks, July 2014

Revision BJanuary 22, 2015

Page 2: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

Calorimeter Time Constant Check

Simple Model

Mass = 6,213 kg (half model)Heat capacity = 1.35E+06 J /KConvective area = 1.96E+06 mm̂ 2 (1/2 model)Conv coef = 3.83E-05 W/mm̂ 2-KHeat load = 20.71 W (half model)

• A simple model consisting of a mass with associated convective area was used for a time constant check. The mass and the convective surface are at the same temperature which increases over time due to applied heat. Model parameters are listed below.

Page 3: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

Simple model compared to calorimeter results

0 20,000 40,000 60,000 80,000 100,00089.7

89.8

89.9

90

90.1

90.2

90.3

90.4

90.5

90.6

Temperature After Step Application of Power

T2481T2489T2495T2406T2500Simple model

Time, seconds

Tem

p, D

eg K

Simple model results are representative of the lower temperature nodes that were selected for the response plot. The gradients (in the detailed model) developed in 40,000 seconds after which the mass heated at a uniform rate. The time constant for gradient development (time to 63.2% of the steady state value) is 15,300 sec or 4.25 hrs.

Steady state results are shown above. High temperatures occur in a fraction of the total volume in the heated region and away from the cooled region.

Page 4: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

Simple Model with Various Shell Convection Coefficients

0 20,000 40,000 60,000 80,000 100,00089.0

89.5

90.0

90.5

91.0

91.5

92.0

Simple Model Temperature After Step Application of Power

H=38.3 W/m^2-K0.5*H nom2*H nmH=0

Time, seconds

Tem

p, D

eg K

0 20,000 40,000 60,000 80,000 100,00089.7

89.8

89.9

90.0

90.1

90.2

90.3

90.4

90.5

Simple Model Temperature After Step Application of Power

H=38.3 W/m^2-K0.5*H nom2*H nmH=0

Time, seconds

Tem

p, D

eg K

The time constant of the simple model response is taken to be the time for 63.2% of the mass temperature change. at 50% of the nominal convective coefficient the time constant is 9.86 hours at 100% of the nominal convective coefficient the time constant is 4.58 hours at 200% of the nominal convective coefficient the time constant is 2.50 hours

Page 5: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

Length of Mini-F-Cal

• The mini-F-Cal model was based on the “dimensions” tab of the Excel file “Heatmini.xlsx” as shown below.

• The specified and modeled length of the calorimeter is 30 cm

as was intended.

Page 6: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

Test Bed External Boundary Conditions• Initially the six sides of the test bed box were constrained to be at 90°K• Based on the gap convection results, external convection could be as low as

49 W/m2-°K– Free convection in the 12 mm gap on the 900 mm diameter calorimeter was 38 W/m2-°K for

an 0.5°K differential and 49 W/m2-°K for a 2°K differential– On the 144 mm diameter ID with a gap of 14 mm convection was calculated to be 40 W/m2-

°K for an 0.15°K differential– Because the fluid is less constrained around the test bed as compared to the gap cases, the

free convection coefficient is expected to be larger than the above cited gap values and 49 W/m2-°K is taken as a minimum value.

• Conduction through the G10 on five sides is equivalent to 20 W/m2-°K (20 to 23.4 mm of G10). Adding convection to this gives 14 W/m2-°K or ~70% of the conduction expected if convection to the Argon pool is high.

• Conduction through the copper matrix is high so the addition of convection to the Argon pool makes a large difference.

It is concluded that external convection cannot be neglected. Additional cases with external convection of 49 W/m2-°K and 98 W/m2-°K have been added to these results.

Page 7: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

Summary of Test Bed Analysis Results

• The conduction across the argon layer will be determined by measuring the heat flux through the G10 layer and the temperature drop across the argon layer.– Heat flux and temperature drop will be measured near the centerline.

0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1.00.0

0.1

0.2

0.3

0.4

0.5

Test Bed Transient Response, 0.5deg Gradient

High H 0.5KHigh H 2 KNom H 0.5 KNom H 2 K

time, hours

Argo

n to

G10

gra

dien

t rati

o

Time required for stability:

The heat flux through the G10 will be calculated from the gradient through the G10. The ratio of the G10 and argon gradients is stable after 0.4 hours for both nominal (low) and high external convection cases.

Page 8: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

Temperature of the Argon Layer• The argon layer

temperature and the copper matrix temperature are sensitive to the external convection coefficient.

• It should be possible to determine the external convection coefficient from the test data.

• Boiling in the argon layer must be avoided.

0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1.090.0

90.5

91.0

91.5

92.0

92.5

93.0

93.5

94.0

Test Bed Transient Response, Argon Layer Temperature on the G10 side

High H 0.5KHigh H 2 KNom H 0.5 KNom H 2 K

time, hours

Argo

n to

G10

gra

dien

t rati

o

If the external convection coefficient is low the argon layer temperature will be higher and boiling may occur. This will increase the heat transfer rate since nucleate boiling is a particularly effective heat transfer mechanism.

Page 9: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

Mini-F-Cal with Conductive Bars• Contact conductance between the bar and the 12 mm OD pipe is

estimated to be larger than or equal to an argon film 0.1 mm thick– Q/ΔT = 2.2 W/°K

• Argon conductivity is 0.1315E-3 W/mm/K• Area in contact is 12π*44 mm2

• Path length is 0.1 mm

– For reference the conduction from the matrix to the tube through the 3x44mm strap is 12.4 W/°K• Copper conductivity is 0.542• Area is 3x44=132 mm2

• Path length is ~ 30 mm (20 mm to the tube and ¼ the distance around the tube

– Contact resistance is modeled by decreasing the conductivity of part of the copper bar near the “tube”. The tube is a region constrained to 77°K

Page 10: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

Nominal Power Level, Cooled only by the LN2 loop

Most of the collimator is near 84 K. The bar could be shortened since most of its length is at the same temperature as the copper matrix.

The only cooling here is from the LN2 loop.

Page 11: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

Operation at 7.5 times Power

The LN2 loop is still at 77°K but 7.5 times the power is applied resulting in a peak temperature of 132 K. Again the only cooling is from the LN2 loop.

Page 12: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

Operation at 7.5xPower with LN2 Loop Cooling and External Wall Cooling by 90°K Argon

Peak temp is 101°K

Page 13: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

Backup Slides

• Test bed results with various outer surface convection coefficients

Page 14: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

14

Thermal Result for an 0.5°K Gradient Across the 12 mm Argon Layer, Net Conductance of the Argon is 3.8 Times the Conductivity of Argon

Node Temp Del T Q centerdeg K deg K W/m̂ 2

4570 91.56Mid Insul 1.05 26.14

4620 90.51Aluminum 0

4670 90.51Argon 0.5 21.13

4720 90.01Copper

Total heat input = 6.75 WHeat into 8 mm Al plate = 1.82 WHeat into 12 mm Argon layer = 1.77 W (21.9 W/m2)Heat out of Argon Layer = 1.67 WRadial loss from Al and Argon 0.14 WHeat lost through base = 4.84 W

72% of the input heat is lost through the base. Most of the rest passes through the Argon

Outer surfaces fixed at 90°K (very high convection coefficient)

Page 15: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

15

Thermal Result for a 2°K Gradient Across the 12 mm Argon Layer, Net Conductance of the Argon is 4.8 Times the Conductivity of Argon

Node Temp Del T Q centerdeg K deg K W/m̂ 2

4570 97.083Mid Insul 5.045 125.36

4620 92.038Aluminum 0.009 105.2

4670 92.029Argon 2.002 105.28

4720 90.027Copper

Total heat input = 31.18 WHeat into 8 mm Al plate = 8.78 WHeat into 12 mm Argon layer = 8.62 W (107 W/m2)Heat out of Argon Layer = 8.26 WRadial loss from Al and Argon 0.49 WHeat lost through base = 22.04 W

70% of the input heat is lost through the base. Most of the rest passes through the Argon

Outer surfaces fixed at 90°K (very high convection coefficient)

Page 16: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

16

Thermal Result for an 0.5°K Gradient Across the 12 mm Argon Layer, Net Conductance of the Argon is 3.8 Times the Conductivity of Argon

Node Temp Del T Q centerdeg K deg K W/m̂ 2

4570 92.07Mid Insul 1.25 28.48

4620 90.82Aluminum -0.1

4670 90.92Argon 0.5 21.16

4720 90.42Copper

Total heat input = 6.05 WHeat into 8 mm Al plate = 2.00 WHeat into 12 mm Argon layer = 1.90 W (23.6 W/m2)Heat out of Argon Layer = 1.72 WRadial loss from Al and Argon 0.32 WHeat lost through base = 4.05 W

67% of the input heat is lost through the base. Most of the rest passes through the Argon

Outer surface convection to 90K is 49 W/m2-°K (nominal convection coefficient)

Page 17: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

17

Thermal Result for a 2°K Gradient Across the 12 mm Argon Layer, Net Conductance of the Argon is 4.8 Times the Conductivity of Argon

Node Temp Del T Q centerdeg K deg K W/m̂ 2

4570 99.66Mid Insul 5.58 138.2

4620 94.08Aluminum 0.01

4670 94.07Argon 2 105.2

4720 92.07

Total heat input = 28.62 WHeat into 8 mm Al plate = 9.72 WHeat into 12 mm Argon layer = 9.35 W (116 W/m2)Heat out of Argon Layer = 8.53 WRadial loss from Al and Argon 1.41 WHeat lost through base = 18.90 W

66% of the input heat is lost through the base. Most of the rest passes through the Argon

Outer surface convection to 90K is 49 W/m2-°K (nominal convection coefficient)

Page 18: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

A tabular summary of test bed results with various external convection values and with 0.5 and 2°K gradients in the Argon layer

External convection High High nominal nominal 2*nom 2*nom

T4570 deg K 91.56 97.07 92.07 99.66 91.75 98.19T4620 (4570-4620 = G10) deg K 90.51 92.04 90.82 94.08 90.70 93.03T4670 (4620-4670 = Al) deg K 90.51 92.03 90.92 94.07 90.70 93.02T4720 (4670-4720 = Argon) deg K 90.01 90.03 90.42 92.07 90.22 91.10T4770 (4720-4770 = copper) deg K 90.01 90.03 90.42 92.07 90.22 91.10

Q4620 Mid insulation W 0.0033 0.0157 0.0036 0.0173 0.0033 0.0160Q4670 Aluminum W 0.0026 0.0132 0.0026 0.0131 0.0025 0.0126Q4720 Argon layer W 0.0026 0.0132 0.0026 0.0131 0.0025 0.0126

Total heat input W 6.750 31.180 6.049 28.622 6.031 28.630Heat into 8mm Al plate W 1.823 8.780 1.997 9.719 1.829 8.975Heat into Argon layer W 1.767 8.620 1.901 9.350 1.749 8.683Heat out of Argon layer W 1.672 8.260 1.719 8.527 1.606 8.048Radial loss from Al and Argon W 0.142 0.490 0.319 1.412 0.245 1.051Lost through base W 4.840 22.040 4.052 18.903 4.202 19.655

Derived resultsQcenter across G10 W/m̂ 2 26.14 125.36 28.48 138.18 26.16 128.00Qcenter across Argon W/m̂ 2 21.13 105.20 21.16 105.18 20.00 100.80Qargon/QG10 = 81% 84% 74% 76% 76% 79%

Qaverage across argon W/m̂ 2 21.93 106.98 23.59 116.04 21.71 107.76

Reduced external convection results in a significant increase in the copper matrix and Argon layer) temperatures.

Reduced external convection changes the ratio of Argon layer to G10 layer heat flux from 81-84% for high coupling to 74-76% for low coupling efficiency.

“High” external convection means the external surface is set at 90°K“nominal” external convection is 49x10-6 W/m2-°K

Page 19: Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015

19

Temperature Drop Across the Argon Layer

0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1.00.0

0.5

1.0

1.5

2.0

2.5

Test Bed Transient Response, Temperature Drop Across the Argon Layer

High H 0.5KHigh H 2 KNom H 0.5 KNom H 2 K

time, hours

deg

K