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Heat transfer of a spray droplet in a PWR pressurizer

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Abstract

Heat transfer rates to spray droplets under conditions corresponding to those of spray transients in a pressurizer of pressurized water reactor (PWR) have been predicted by a simple droplet model with internal thermal resistance and partial internal mixing. In those processes, the temperature distributions in the droplet have been obtained using the integral method, and the physical properties of the saturated steam-hydrogen gas mixture surrounding the droplets are estimated applying the concept of compressibility factor and using appropriate correlations. Results have been provided for the temporal variations of total heat flux with its convection and condensation heat transfer components, dimensionless droplet bulk temperature and droplet flight distance. The effects of ambient pressure, initial droplet size, concentration of hydrogen gas in the mixture, initial injection velocity, and spray angle on the heat transfer of spray droplets have been discussed.

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Abbreviations

A :

Cross-sectional area of a droplet

Bi :

Biot number (=h t R/k i )

C D :

Drag coefficient

C p :

Specific heat at constant pressure

D :

Derivative with respect to τ(=d/dτ)

D 12 :

Mass diffusivity of steam in a mixture

g :

Gravitational acceleration

H fg :

Latent heat of condensation

h c :

Convection heat transfer coefficient

h t :

Apparent heat transfer coefficient

J s :

Mass flux of steam

k :

Thermal conductivity

M :

Molecular weight

m :

Mass of a droplet

Nu :

Nusselt number (=2h c R/k m )

P :

Pressure

P gm :

Logarithmic mean gas pressure difference

Pr :

Prandtl number (=μ m C ipm/k m )

qL :

Sensible heat flux to a droplet

qs :

Latent heat flux to a droplet

qt :

Total heat flux to a droplet

\(\bar R\) :

Universal gas constant

Re :

Reynolds number (=2ρ m WR/μ m )

γ:

Radial distance in spherical coordinate

Sc :

Schmidt number (=μ/D 12 ρ m )

Sh :

Sherwood number (=2βR/D 12)

T :

Temperature

t :

Time

U :

Horizontal velocity component

V :

Vertical velocity component

\(\bar R\) :

Molar specific volume

ν:

Specific volume

W :

Velocity of a droplet (=U 2+V 2)1/2)

x, y :

Cartesian coordinates

Y :

Flight distance

y i :

Volume fraction of each component in the mixture

Z :

Compressibility factor

α:

Thermal diffusivity

β:

Mass transfer coefficient

Θ b :

Dimensionless droplet bulk temperature (=T b -T 0)/(T -T 0)

θ:

Transformed temperature in dimensionless form

μ:

Dynamic viscosity

ξ:

Dimensionless radial distance in spherical coordinate

ρ:

Density

τ:

Dimensionless time (=α l t/R 2)

ϕ:

Spray angle

ω:

Acentric factor

b :

Bulk

c :

Critical value

g :

Noncondensable gas

i :

At the interface between the droplet and the mixture

l :

Droplet

m :

Mixture

o :

Initial condition

r :

Reduced value

s :

Saturated steam or droplet surface

∞:

Ambient

o :

Low pressure

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Jo, JC., Lee, SK. & Shin, WK. Heat transfer of a spray droplet in a PWR pressurizer. KSME Journal 5, 130–139 (1991). https://doi.org/10.1007/BF02953612

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