Heat Pipes, Fifth Edition

Nomenclature

A c

Circumferential flow area

A w

Wick cross-sectional area

C p

Specific heat of vapour, constant pressure

C v

Specific heat of vapour, constant volume

D

Sphere density in Blake-Kozeny equation

H

Constant in the Ramsey-Shields-Eotv s equation

J

4.18 J/g mechanical equivalent of heat

K

Wick permeability

L

Enthalpy of vapourisation or latent heat of vapourisation

M

Molecular weight

M

Mach number

M

Figure of merit

N

Number of grooves or channels

Nu

Nusselt number

Pr

Prandtl number

P

Pressure

?P

Pressure difference

?Pcmax

Maximum capillary head

?Pl

Pressure drop in the liquid

?Pv

Pressure drop in the vapour

?Pg

Pressure drop due to gravity

Q

Quantity of heat

R

Radius of curvature of liquid surface

Ro

Universal gas constant = 8.3 10 3 J/K kg mol

Re

Reynolds number

Re r

Radial Reynolds number

Re b

A bubble Reynolds number

S

Volume flow per second

T

Absolute temperature

T c

Critical temperature

T v

Vapour temperature

?T s

Superheat temperature

T w

Heated surface temperature

V

Volume

V c

Volume of condenser

V R

Volume of gas reservoir

W e

Weber number

a

Groove width

a

Radius of tube

b

Constant in the Hagen-Poiseuille Equation

c

Velocity of sound

d a

Artery diameter

d w

Wire diameter

f

Force

g

Acceleration due to gravity

g c

Rohsenhow correlation

h

Capillary height, artery height, coefficient of heat transfer

k

Boltzmanns Constant = 1.38 10 ?23 J/K

k w

Wick...

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