Summary - Complete - Heat Transfer all Important Equations PDF

Title Summary - Complete - Heat Transfer all Important Equations
Course Fluid Flow, Thermodynamics and Heat Transfer
Institution University of Birmingham
Pages 3
File Size 105.2 KB
File Type PDF
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Summary

Heat transfer all important equations...


Description

Equation Sheet for Heat Transfer These are the main equations you should know. You will not be given this sheet for class tests or examination. This is meant as a guide to aid your revision and the list is by no means exhaustive.

General

H  mc P TB  TA   mc P T

(for mass)

H  Q  mC cPC TC1  TC 2 

(for mass flow)

And heat/energy balances

Conduction Q  kA

Q

T1  T2 

(single slab)

x

T T   x  RT    kA 

(slabs in series)

Know how to determine resistances in parallel

T  T2 Q  k 2L 1 r  ln  2   r1 

Q

2 L(T1  T3 ) r r ln( 2 ) / ka  ln( 3 ) / k b r2 r1

(single cylinder)

(cylinders in series)

Convection Nu = f(Gr, Pr) Natural Convection Nu = f(Re, Pr) Forced Convection

Nu 

hL k

Nusselt number

cp

Pr 

Prandtl number

k

Re 

Lu

Reynolds number



Know how to use the exact and MacAdams (approximate formulas) see pages 3 – 5 Convection notes Know how to use Sieder and Tate and Dittus-Boelter equations

d 2  d1

de =

equivalent hydraulic diameter for non circular channels

-

Q  h A T

Newtons Law of heating/cooling

1  do 1      U o  hi d i ho 

Overall heat transfer coefficient for thin walled pipes

Q  U o Ao TLM

Overall Heat transfer rate across an object

LMTD   TLM 

Ao = πdoL,

T 2  T1  T  ln  2   T1 

Long mean temperature difference

Surface area of a pipe

Know difference between co-current and countercurrent flow Velocity profiles in laminar and turbulent flow

Radiation

max  T  C3

Weins displacement Law - Third radiation constant C3

Eb    T 4

Stefan-Boltzmann Law for black body

Qr A

 Eb1  Eb 2   (T1 4  T 24 ) or qb = T14 - T24

Radiative heat exchange (flux) between 2 black body plates

 

E and a  E Eb Eb

so a  

E    E b      T4

q1 2 

1 1  1

1

if

A1  A2

 2 1

then

Kirchoff’s Law

Stefan-Boltzmann for Grey (real) bodies

   ( T14  T24 )

Radiative heat flux between 2 grey plates

q1 2  1    ( T14  T24 )

Know where view factors (F) and Hottel coefficients ( 1 2 ) are included in Stefan-Boltzmann equations for black and grey bodies

Eg  g  As   Tg4

Radiation of gases

Gs ,0  Sc  f  cos 

Extraterrestrial radiation...


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