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ASTM - Intensive Quenching Systems - Engineering and Design 2010 - N I Kobasko, M A Aronov, J A Powell, G E Totten

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CHAPTER 2 n TRANSIENT NUCLEATE BOILING AND SELF-REGULATED THERMAL PROCESSES 27

where:

R cr is a critical size of a bubble which is capable to grow and

function;

r is surface tension (N/m);

T S is a saturation (boiling) temperature (K);

r * is latent heat of evaporation (J/kg);

r 00 is vapor density (kg / m 3 ); and

DT ¼ T Sf – T m is wall overheat.

Active nucleating centers are the basic carriers that

remove heat from a surface and transfer it to a cooler bath,

as explained by Dhir [2, p. 372]: After initiation, a bubble

continues to grow (in a saturated liquid) until forces cause

it to detach from the surface. After departure, cooler liquid

from the bulk fills the space vacated by the bubble, and the

thermal layer is re-formed. When the required superheat is

attained, a new bubble starts to form at the same nucleation

site. Bubble dynamics include the processes of growth,

bubble departure, and bubble release frequency, which

includes time for reformation of the thermal layer (induction

period). The bubble acts like a pump, removing hot liquid

from the surface and replacing it with cooler liquid.

This mechanism is the essential factor causing the high

intensity of heat transfer during boiling, and the bath temperature

essentially has no effect [1,2]. Therefore, it is necessary

for the heat flux density during boiling to relate to a

difference of T Sf – T S ,butnottoT Sf – T m , which can lead

to large errors since

T Sf T S << T Sf T m :

These calculations were conducted at the saturation

temperature of a liquid. However, it is important to determine

the effect of underheat on the inner characteristics of

the boiling process. Underheat is defined as a difference in

temperatures between the saturation temperature and the

bath temperature (bulk temperature):

DT uh ¼ T S T m : ð6Þ

The effect of underheat on the maximum diameter

d max of bubbles and their departure frequency f, and also

on the average vapor bubble growth rate W 00 during boiling

of underheated water at normal pressure, is shown in

Fig. 5.

From Fig. 5, when underheating increases, the bubble

departure diameter decreases and the release frequency

increases. The average growth rate of vapor bubbles also

increases. All of these facts are probably also true for partial

nucleate boiling. Shock boiling and developed nucleate boiling

close to transition boiling have, as yet, not been exhaustively

studied.

When pressure increases, the bubble departure diameter,

bubble release frequency, and average vapor bubble

growth rate decrease (see Fig. 6).

These characteristics will be used for the computation

of temperature fields during steel quenching.

Tolubinsky obtained the following generalized equation

for the calculation of a heat transfer coefficient during nucleate

boiling:

Nu ¼ 75K 0:7 Pr 0:2 ;

where: qffiffiffiffiffiffiffiffiffiffiffiffiffi

Nu ¼ a r

k gðr 0 r 00 Þ

is the Nusselt criterion (number);

a

Pr ¼ v a

is the Prandtl number;

ð7Þ

Fig. 5—The effect of underheat upon the maximal diameter

d max (1), bubble release frequency f (2), and average vapor bubble

growth rate W 00 (3) at boiling of underheated water (P ¼ 0.1

MPa) [1].

is the heat transfer coefficient during nucleate boiling

(W/m 2 K);

k is the heat conductivity of the liquid (W/mK);

r is the surface tension (N/m);

g is gravitational acceleration (m/s 2 );

r 0 is liquid density (kg/m 3 );

r 00 is vapor density (kg/m 3 );

q is heat flux density (W/m 2 );

r * is latent heat of evaporation (J/kg);

W 00 is vapor bubble growth rate (m/s);

m is kinematic viscosity (m 2 /s); and

a is thermal diffusivity of liquid (m 2 /s).

In the expanded form, Eq 7 can be rewritten as follows:

a

k

rffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffi

r

q 0:7

a

0:2:

gðr 0 r 00 ¼ 75

Þ r r 00 w 00 v

Fig. 6—The effect of pressure upon bubble parameters at boiling

of underheated water (DT uh ¼ 20K): solid dots indicate bubble

departure frequency; open dots show bubble departure diameter;

lower graph plots vapor bubble growth [1].

ð8Þ

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