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80

CHAPTER 4

that there is an interfacial resistance to heat flow since, in point of fact, at a discontinuity in temperature the temperature gradient is infinite. A theory of the Kapitza discontinuity based on considerations of the phonon spectrum in the solid and the liquid predicts n = 4; experimental values lie mainly in the range 3 + 0.5 (Sciver, 1986). The experimental values of the coefficient a are scattered; a suitable value for purposes of rough estimation is a = 40 mW cm-2 K-3 when n = 3 (Sciver, 1986).

As time progresses, the heater temperature gradually increases, approaching at long enough times proportionality to the square root of the elapsed time. In this regime, which is clearly visible for the smaller heat fluxes in Fig. 4.23, the rate-determining heat transfer process is transient conduction through the heated layer of liquid helium adjacent to the heater surface. After a time, the heat being transferred to the helium causes bubbles to appear, and the dominant mode of heat transfer becomes nucleate boiling. For small heat fluxes, this nucleate boiling may persist indefinitely. For larger fluxes, it ends when there is a transition to film boiling accompanied by a large increase in the heater temperature. This transition is called takeoff.

The time tf to takeoff as a function of the constant heat flux q has been measured by several workers and the measurements compiled by Schmidt (1982) (see Fig. 4.24). The near constancy of qt1/2f suggested to Schmidt the following elementary theory of transient heat transfer in saturated helium. According to ordinary diffusion theory, when the flux entering a half-space is suddenly clamped at a constant value q, the temperature rise ∆T at the front face is given by

T= (4q2t/ pkS )1/2

(4.11.2)

where t is the elapsed time since the heater was energized, k is the thermal conductivity of helium and S is its volumetric heat capacity. The heat introduced per unit face area during the time t is qt. If this heat is absorbed in a thin layer of

Figure 4.24. The time to takeoff as a function of the constant heat flux according to Schmidt (1982). (Redrawn from an original provided courtesy of the International Institute of Refrigeration.)

Boiling Heat Transfer and Cryostability

81

helium of thickness d in which the temperature rise is uniform at the value given in Eq. (4.11.2), then S T d = qt, so that

d = (πkt/4S)1/2

(4.11.3)

Schmidt postulates that takeoff occurs when the heat transmitted qt equals the latent heat Lδ of the heated layer, for at that time he supposes that there is enough heat present to vaporize the entire heated layer. Thus

qt f1/2 = (πk/4S)1/2L = 39 mW cm-2 s1/2

(4.11.4)

(k/S = 2.84 x 10-8 m2/s and L = 2.59 J/cm3 according to Arp and McCarty (1989). The curve in Fig. 4.24 corresponds to a value of qtf1/2 = 51 mW cm-2 s1/2 ; its rather

good agreement with the experimental facts supports Schmidt’s picture of what is going on. (N.B.: Schmidt (1978; 1982) first used a factor of 2, later a factor of π/2 in Eq. (4.11.4) instead of the factor (π/4)1/2.)

Armed with Schmidt’s formula (4.11.4), we can attack the following problem. If an intense disturbance lasts for a short time t, what is the maximum heat it can produce without causing a transition to film boiling? The maximum allowable heat input per unit area H is clearly that which just makes tf = t. Now since q = H/t,

we find from Eq. (4.11.4) that

 

H = (πk/4S )1 / 2L(t)1/2

(4.11.5)

Eq. (4.11.5) is based on neglect of any Joule heat produced during transient heat transfer. This is a satisfactory assumption for short enough times t because H varies as (t)1/2 whereas the Joule heat varies as t. Table 4.1 shows for several values of t the heat H calculated from Eq. (4.11.5) and the maximum Joule heat per unit surface area (ρcuJ2A/fP)t for the numerical example of Section 4.8. In this example, for the times given, the neglect of the Joule heat is roughly justified.

The time t can be estimated for the conceptual model of conductor slippage introduced in Section 4.8. If the conductor slips freely, its motion is restrained only

by its inertia. The time to

reach mechanical equilibrium is of the order

 

Table 4.1. Comparison of the Allowable Heat

 

 

H with the Joule Heat

 

 

 

 

 

 

t

H

(ρcu J2A /fP)t

 

(s)

(J/m2)

(J/m2)

 

10–6

0.510

0.0138

 

 

10–5

1.61

0.138

 

 

10–4

5.10

1.38

 

82

CHAPTER 4

(b2/a)(δ/Y )1/2, where d is the density of the conductor (8960 kg/m3 for copper,

Southwell, 1969). This time turns out to be about 9 µ s for b = 5 mm and a = (π/4)1/2D = 0.71 mm. The total Joule heat H(A/P)b produced in a 5-mm span

is then about 1.5 µ J. This heat can be added to the MPZ energy 16.6 µ J, since the latter value is predicated on the film-boiling heat transfer coefficient. In this case, transient heat transfer slightly improves the stability of the conductor; its neglect is thus slightly conservative.

5

Normal Zone Propagation

5.1. EXACT CALCULATION OF THE PROPAGATION VELOCITY

When the current lies beyond the minimum propagating current (see Fig. 4.7), local normal zones whose formation energy exceeds the minimum quench energy grow. Their central temperature approaches the temperature T2 of point 2 in Fig. 4.8 and their edges propagate outwards. The situation is much the same as shown in Fig. 4.6b, except that now t4 is the earliest time and t1 the latest. In most cases, the propagation is uniform, i.e., the velocity is constant and the temperature profile at the edges of the normal zone does not change its shape with time.

The propagation velocity is comparatively easy to measure. One method is to measure the voltage produced by the normal zone as a function of time. In well-cooled magnets in which the central temperature T2 is less than about 20 K, the resistivity of the matrix is nearly independent of temperature, and the rate of increase of the normal-zone voltage is proportional to the propagation velocity. In uncooled magnets, the central temperature of an expanding normal zone keeps on rising as does the resistivity, and the contribution to the voltage from the center of the normal zone becomes disproportionately large. In such a case, voltage measurement is not a reliable way to measure the propagation velocity. A second way, free from this defect, is to time the flight of the normal–superconducting front between two voltage taps.

Owing to the complexity of boiling heat transfer, the propagation velocity is measured in order to determine the minimum propagating current. A typical series of measurements provides points on the curve of propagation velocity versus transport current (Fig. 4.7). The minimum propagating current is then determined by interpolation. The part of the curve so measured can be used to extract information about heat transfer during normal zone growth or shrinkage. Several attempts of this kind have been made; in order to discuss them, we must first calculate the

83

84 CHAPTER 5

propagation velocity in order to determine its dependence on the various parameters of the conductor.

The basic equation from which we start is Eq. (4.4.2), which describes the left-hand edge of a normal zone, i.e., the edge that propagates from right to left. Again, to obtain a solvable problem, we use Newton’s law of cooling and assume k and S to be independent of temperature. We again introduce the variable s = k(dT/dz) and finally employ the special units of Section 4.7. The result is the first-order ordinary differential equation

s(ds/dτ) – vs + ai2g(τ) τ = 0

(5.1.1)

the solution of which must obey the boundary conditions s(0) = 0 and s (ai2) = 0 (since τ2 = ai2).

Altov et al. (1973) were the first to solve the problem just formulated using finite differences. Later, the author gave an analytical solution to the problem (1979, “Analytic Solution”). The results of these exact calculations (in the special units of

Section 4.7) is the functional dependence of v on a and i: v = F (a,i). Remembering that (rcuJ 2/f )/(hP tc/A ) = ai 2, we can write

v = [(rcu J 2/f )/(hP tc /A)]1/2[F(a,i)/a1/2i]

(5.1.2)

which becomes in ordinary units

 

 

v = (k/S )(hP/kA)1/2[(rcu J 2/f )/(hP tc/A)]1/2[F (a,i)/a1/2i]

 

= (2λ J /S)(ρ

cu

k/fτ

)1/2 · [F(α ,i)/2α1/2]

(5.1.3)

c

c

 

 

Shown in Fig. 5.1 is the second factor in Eq. (5.1.3) plotted versus i with a as a parameter. It approaches 1 when i approaches 1 for all a. When a →∞,i.e., when h 0 (an uncooled superconductor), F (a,i)/2a1/2ci 1/2/2, where c is related to i by the equation (Dresner, 1980, “Propagation”):

[c/(4 – c2)1/2]arctan[c(4 – c2)1/2/(2 – c2)] + 2 In c = ln[i/(1 – i)]

(5.1.4)

The curve ci1/2/2 is the uppermost curve shown in Fig. 5.1. It alone extends down to i = 0. All the other curves cross the axis v = 0 at values of i satisfying the equal-area requirement ai2 = 2 – i. Between this value of i and the Stekly value, which satisfies ai2 = 1, initial normal zones collapse by cold-end recovery, the flanks of the zone moving inwards with the (negative) velocity v. As i approaches the Stekly value from above, v .Below the Stekly value of i, all points of the initial normal zone recover simultaneously, and the notion of propagation is inapplicable. (N.B.:

In evaluating the left-hand side of Eq. (5.1.4), use the principal value of the arctan lying in the interval (0,p).)

Normal Zone Propagation

85

Figure 5.1. The second factor in Eq. (5.1.3) plotted versus i: it gives the dependence of thepropagation velocity on the current.

The first factor on the right-hand side of Eq. (5.1.3) (callit v*)can be simplified for a matrix material obeying the Wiedemann–Franz law, Eq. (2.9.1). Since the thermal conductivity of the matrix is typically >> than that of the superconductor, k/f= kcu and the first factor in Eq. (5.1.3) becomes

v

*

= (2λ J /S)[(L

T

b

/(T

c

– T

b

)]1 / 2

(5.1.5)

 

c

o

 

 

 

 

 

where we have given the quantities ρcu and kcu, which have been assumed independent of temperature, the values they have at the ambient temperature Tb. Using the figures given in the example of Section 4.8, we find v* = 86.8 m/s; since in this example a = 27.4 and i = 0.6, we see from Fig. 5.1. that F(α,i)/2α1/2= 0.32, so that v = 27.8 m/s. This single example gives some idea of the order of magnitude of the propagation velocity. But it can vary widely depending on the circumstances. In the new high-temperature superconductors, it can be as little as a few mm/s, whereas in the cabled conductor of the Superconducting SuperCollider 17-m dipoles, it was as much as several hundred m/s.

5.2.APPROXIMATE CALCULATION OF THE PROPAGATION VELOCITY

The implicit relation between c and i in Eq. (5.1.4) is inconvenient when one wishes to undertake repetitive calculations even on an electronic computer. The analytic solution of reference (Dresner, 1979, “Analytic solution”) for F (a,i) involves an even more complicated relation than that of Eq. (5.1.4) and greater inconvenience. A simple, explicit, and quite accurate approximate result for F (a,i) can be arrived at by replacing in Eq. (5.1.1) the three-part curve (4.7.2) for g(τ) by the two-part curve

86

CHAPTER 5

= 0

τ < 1 – i/2

g(τ)

(5.2.1)

= 1

τ > 1 – i/2

This replacement has the desirable property that the differences in area of the right-hand and left-hand stippled regions in Fig. 4.15 are the same for the three-part g(τ) of Eq. (4.7.2) as for the two-part g(τ) of Eq. (5.2.1), namely, αi2(αi2 – 2 + i)/2. Thus the minimum propagating (v = 0) value of i is the same in both cases.

When τ < 1 – i/2 and g = 0,

s = l+t

(5.2.2)

where l+ is the positive root of the quadratic equation

 

l2 v l – 1 = 0

(5.2.3)

(Remember, we are calculating the velocity of the left-hand edge of a normal zone for which s = k(dT/dz) > 0.) When t > 1 – i/2 and g = 1,

s = m+(ai

2 t)

(5.2.4)

where m+ is the positive root of the quadratic equation

 

m2 + v m

1 = 0

(5.2.5)

The partial solutions (5.2.2) and (5.2.4) satisfy the boundary conditions s(0) = 0 and s(αi2) = 0, as they should. They must be equal at t = 1 – i/2, and this condition gives the result

v = (C – 1)/C1/2 where C = [αi2 – (1 – i/2)]/( 1 – i/2)

(5.2.6)

Since this result obtains in special units,

F(α,i) = (C – 1)/C1/2

(5.2.7)

Figure 5.2 shows a plot of the approximate value of F(α,i)/2α1/2 plotted versus i with the same values of as a parameter as used in Fig. 5.1. The agreement is excellent over most of the range of i, with serious deviations only near i = 1. According to the author (Dresner, 1979, “Analytic solution”), considerable im-

provement in agreement can be achieved by applying the empirical factor 1 + 0.561a–1.45 to the result calculated from Eq. (5.2.6).

Normal Zone Propagation

87

Figure 5.2. The approximate value of the second factor in Eq. (5.1.3) plotted versus i [cf. Eqs. (5.2.6) and (5.2.7)].

5.3. COMPARISON WITH EXPERIMENTS OF IWASA AND APGAR

The curves in Fig. 5.1 can be compared with experimental propagation velocities in the following way. The intersections of the curves with the i-axis are the dimensionless minimum propagating currents corresponding to the various values of the Stekly number a. Experimental values of the minimum propagating current can thus be used to determine a. Then we can use the value of a so determined to calculate the propagation velocity as a function of i using Eq. (5.1.3) and the data in Fig. 5.1 or Eq. (5.2.7).

Straightforward as this procedure seems, it fails to reproduce the experimentally measured propagation velocities. The experimental and calculated curves have the same intercept on the i-axis, of course, but the theoretical curve is usually several times steeper than the experimental curve. This difficulty is not eliminated by use of a three-part boiling curve and temperature-dependent thermophysical properties, as extensive numerical calculations have shown (Dresner, 1976).

I gave a hint at the resolution of this difficulty, when I became convinced “that steady-state heat transfer coefficients are inadequate to describe the growth of normal zones” (Dresner, 1976). Accordingly, I introduced ad hoc corrections for transient heat transfer that raised the heat transfer coefficient at the propagating wave front but allowed it to approach the steady-state value far behind. Agreement was much improved, and I concluded this work by recommending “a velocity-de- pendent correction that increases with velocity.” Later, I used a velocity-dependent correction that raised heat transfer for expanding zones and lowered it for collapsing zones (Miller et al., 1977). Such a correction slowed both expansion and collapse; thus it decreased the slope of the curve of v versus i in the neighborhood of the minimum propagating current.

This idea proved right: experiments by Iwasa and Apgar (1978) identified the growth and collapse of the vapor film blanketing the conductor surface as the source

88 CHAPTER 5

of the velocity-dependent heat transfer. When the normal zone is expanding, the vapor film forms at the advancing wave front. The latent heat of formation is absorbed from the metal, slowing the rate of advance of the front. When the normal zone is contracting, the vapor film condenses at the retreating wave front. The latent heat of the film is then released to the metal, slowing the rate of retreat of the front.

Iwasa and Apgar measured the instantaneous temperature of a helium-cooled copper plate as a function of heat flux. They expressed the heat flux as a sum of two terms, qs (t), the steady-state term, and a(τ)(dT/dt), a term proportional to the time rate of change of the temperature. From their measurements, they obtained the temperature-dependent coefficient a (τ). By fitting curves of propagation velocity versus transport current measured by Miller et al. (1977), I was also able to obtain the coefficient a (τ) (Dresner, 1979, “Transient heat transfer”). The agreement between these latter values and those directly measured by Iwasa and Apgar was excellent. Tsukamoto and Miyagi (1979) and Nick, Krauth, and Ries (1979)

performed virtually identical analyses,

using Iwasa and Apgar’s transient term

a(τ)(dT/dt) to fit measured velocities of

propagation.

The particular form chosen by Iwasa and Apgar to represent their transient

correction, namely, a(τ)(dT/dt), makes correcting the propagation velocity relatively simple. If one adds this term to q in the fundamental Eq. (4.4.1), one finds that the term a(τ)(dT/dt) can be combined with the left-hand side and has the sole effect of increasing the volumetric heat capacity S by Pa/A. One can therefore use the formulas previously derived, e.g., Eq. (5.1.3), merely by increasing S.

5.4. EFFECT OF TRANSIENT HEAT TRANSFER

The formation and decay of the vapor film is a relatively slow process and the work of Iwasa and Apgar applies only for relatively long transits of the front past a fixed point. In the experiments of Miller et al. (1977), which could be fitted well using the Iwasa–Apgar correction, this transit time was of the order of 10 ms. Judging from Steward’s data in Fig. 4.23, we expect the heat transfer coefficient that controls the motion of the front to be that of film boiling. It is worth noting that the Iwasa–Apgar correction affects both the positive (propagation) and negative (cold-end recovery) velocity.

When the time of transit is much shorter than 10 ms, we expect the heat transfer coefficient that controls the motion of the front to be higher than that of film boiling because of the transient heat transfer processes discussed in Section 4.11. In the experiments of Funaki et al. (1985), the transit time was of the order of a few tenths of a ms. If we fit Eq. (5.1.3) to the data of Funaki et al. by suitably choosing the heat transfer coefficient, we find that it lies in the range 0.5–1.5 W cm-2 K-1 when v is in the range 5–20 m/s. This is larger than the film boiling heat transfer coefficient by roughly a factor of 10 and is typical of the lower left-hand corner of Steward’s diagram, Fig. 4.23.

NormalZone Propagation

 

89

Table 5.1. Summary of the Agreement of Various Theories with the

 

Data of Funaki et al.

 

 

 

 

 

Author

Assumed mechanism a

Agreement

Reference

Dresner

Constant adjustable

Good with suitably

(1979, “Analytic

 

parameters S, h

chosen parameters

Solution”)

Lvovsky and Lutset

D + S

Poor

(1982)

Nick, Krauth, and Ries

N+ S + I

Good

(1979)

Funaki et al.

D +N

Good

(1985)

aD = transient conduction heattransfer; N = metastable nucleation;

S = steady-state film boiling; I = Iwasa–Apgar correction.

Funaki et al. and the authors they quote (Lvovsky and Lutset (1982); Nick et al. (1979); Dresner (1979), “Analytic solution”) undertook rather laborious computations, some numerical and some analytic. The bases of all these computations were not the same. Table 5.1 summarizes the agreement of the various theories with the experimental data presented by Funaki et al. in their Fig. 4 (redrawn here as Fig. 5.3). Probably the simplest thing to do in practical circumstances is to use Eq. (5.1.3)

Figure 5.3. A comparison of propagation data of Funaki et al. (1985) with the theories of various authors (cf. Table 5.4). (Redrawn from an original appearing in Funaki et al. (1985) with permission of Butterworth -Heineman, Oxford, England.)