enzo palmieri the problem of heat transfer at liquid helium temperatures 1st tuesday

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Thermal Boundary Resistance Enzo Palmieri 1,2 , A.A. Rossi 1 , R. Vaglio 3 1 Legnaro National Laboratories of the INFN 2 Università degli Studi di Padova 3 Università degli Studi di Napoli

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Page 1: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

Thermal Boundary Resistance

Enzo Palmieri1,2, A.A. Rossi1, R. Vaglio3

1 Legnaro National Laboratories of the INFN2 Università degli Studi di Padova3 Università degli Studi di Napoli

Page 2: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

RS = RBCS+ RRes

Page 3: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

0.2 0.3 0.4 0.5 0.6

1E-6

1E-5

1E-4

RS Nb 122 After ATM Annealing

f(T) @ 2MV/m FitRs1 (User) Fit of Sheet1 Rs

RS [

]

1/T [K-1]

Model FitRs1 (User)

Equation C+(x*A*exp(-B*x))/((1+exp(-B*x))^2)

Reduced Chi-Sqr 3.55369E-13

Adj. R-Square 0.99425

Value Standard Error

Rs A 0.00367 4.32631E-4

Rs B 14.47994 0.51509

Rs C 1.22522E-6 3.56914E-7

Page 4: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday
Page 5: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday
Page 6: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

Qo

Eacc [Mv/m]

5 10 20 25

Cons

tant

fiel

d

T = 4.2 K

T = 1.8 KCo

nsta

nt p

ower

108

109

1010

1011

120 m

W

Page 7: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

Constant W means that, apart Eacc only T is changing

Constant Eacc means that both T and W are changing

Q is function of 3 variables (T, Eacc, W), and only 2 of them are independent

Page 8: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

0.2 0.3 0.4 0.5 0.61E-7

1E-6

1E-5

RS Nb 122 After 3rd UHV Annealing

100 mW R

s fit

Rs

[]

1/T [K-1]

Model Rs (User)

Equation C+(x*A*exp(-B*x))/((1+exp(-B*x))^2)

Reduced Chi-Sqr 7.85399E-15

Adj. R-Square 0.99727

Value Standard Error

Rs

A 0.00265 2.52241E-4

B 17.57752 0.36563

C 7.37002E-8 3.96425E-8

Page 9: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday
Page 10: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

If we cooled the cavity in 3He instead then in 4He, should we wait a different RRES?

Page 11: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

.. in other words, RRES depends on heat transfer to Liquid He and not only on Nb material?

Page 12: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

Rs vs 1/T (termometro Ge)

0,25 0,30 0,35 0,40 0,45 0,50 0,551E-7

1E-6

1E-5

25 mW 50 mW 75 mW 100 mW 125 mW 150 mW 175 mW 200 mW 400 mW 600 mW 1000mWR

s [

]

1/T [K-1]

Termometro Ge

Page 13: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday
Page 14: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

You have the choice:

• One curve of RS(T) at constant Eacc

• A family of curves of RS(T) at constant W

Page 15: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

R =RS (T) and Q=Q (Eacc),

so we can

join the 2 curves into 1 graph

Page 16: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

0 2 4 6 8 10 12 14107

108

109

@ 4.2K @ 1.8K 25 mW 50 mW 75 mW 100 mW 125 mW 150 mW 175 mW 200 mW 400 mW 600 mW 1000mW

Q

Eacc

[MV/m]

Nb117

Page 17: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

Rs vs 1/T vs P (Cernox X63398)

Page 18: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday
Page 19: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

Masked data

Page 20: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

Rs vs 1/T [P=100mW]

0.20 0.25 0.30 0.35 0.40 0.45 0.50 0.55 0.6010-7

10-6

10-5

Termometro: Cernox X62101

Rs(P=100mW)

1/T

Rs

[]

1/T [K-1]

1/T

At -point:

Rs = 1.350810-7

T = 0.039K

{

Nb123

Page 21: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

Kapitza conductance

=

This quantity has a strong Tn temperature dependence with n varying betwen 2 and 4

NbRF

field

s h𝐾 0

Liquid He

Page 22: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

Whenever we neglect the jump at Tl, we

extract a false value of the strong

coupling factor S

𝑅𝐵𝐶𝑆=𝐴𝑇𝑒− 𝒔2𝑇𝐶

𝑇

Page 23: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

)(2

exp)(00

2

0 TT

sT

T

ATTR C

BCS

000

2

0 12

exp)(T

T

T

sT

T

ATTR C

BCS

00

2

0 2exp)(

T

sT

T

ATR C

BCS

𝒔𝒎𝒆𝒂𝒔=𝒔 (𝟏−∆𝑻𝑻 𝟎

)

Page 24: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

What often we forget is that…

RS = RBCS + RRes

is an approximation

valid only at zero-field

Page 25: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

000

2

0 12

exp)(T

T

T

sT

T

ATTR C

BCS

) exp[

Page 26: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

RS (T+ DT) = f(DT/T2) RBCS + RRes

Page 27: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

0 2 4 6 8 10 12 14107

108

109

@ 4.2K @ 1.8K 25 mW 50 mW 75 mW 100 mW 125 mW 150 mW 175 mW 200 mW 400 mW 600 mW 1000mW

Q

Eacc

[MV/m]

Nb117

Page 28: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

0 2 4 6 8 10 12 14107

108

109

@ 4.2K @ 1.8K 25 mW 50 mW 75 mW 100 mW 125 mW 150 mW 175 mW 200 mW 400 mW 600 mW 1000mW

Q

Eacc

[MV/m]

Nb117

Page 29: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday
Page 30: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday
Page 31: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

the Q-factor decreases linearly with W,

but at a certain point it becomes almost

constant!

Page 32: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

The critical power where the losses change slope do correspond to the He boiling nucleation?

Page 33: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday
Page 34: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

0 1 2 3 4 5 6 7 8 9 10106

107

108

109

Nb 122 After ATM Annealing

4,2K f(T) 1,8K

Q

EAcc

[MV/m]

Page 35: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday
Page 36: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

Is it possible that

He-II will have memory of the

boiling nucleation of He-I ?

Page 37: Enzo palmieri  the problem of heat transfer at liquid helium temperatures 1st tuesday

1.8 K is very close to T ,l

so at 1.8K rn is ~34%