To allow easier access to formulae we commonly refer to within various topics and as a time saver when wanting to generate them in LaTex for discussions, I propose this thread as a convenient place to store useful formulae (to copy and paste as appropriate within threads).
Ouabache
Dec4-05, 03:54 PM
Maxwell's Equations - Integral Form
Gauss' Law for Electricity
\epsilon_o \oint E \cdot dA = \sum q
Ampère’s Law
\oint B\cdot ds =\mu_o\int J \cdot dA+ \mu_o \epsilon_o \frac{d}{dt} \int E \cdot dA
Faraday's Law of Induction
\oint E \cdot ds = -\frac{d}{dt}\int B\cdot dA
Gauss' Law for Magnetism
\oint B \cdot dA = 0
alternate forms see ref1 (http://en.wikipedia.org/wiki/Maxwell's_equations), ref2 (http://hyperphysics.phy-astr.gsu.edu/hbase/electric/maxeq.html)
"Maxwell's Equations are the set of four equations, attributed to James Clerk Maxwell (written by Oliver Heaviside), that describe the behavior of both the electric and magnetic fields, as well as their interactions with matter." ref (http://en.wikipedia.org/wiki/Maxwell's_equations)
Ouabache
Dec5-05, 09:29 PM
Maxwell's Equations - Differential Form
Gauss' Law for Electricity
\nabla \cdot E = \frac{\rho}{\epsilon_0}
Ampère’s Law
\nabla \times B = \mu_0 J + \mu_0 \epsilon_0 \frac{\partial E}{\partial t}
Faraday's Law of Induction
\nabla \times E = -\frac{\partial B}{\partial t}
Gauss' Law for Magnetism
\nabla \cdot B = 0
The above differential and integral forms (previous post) may be used in the absence of magnetic and polarizable media.
Alternate forms see ref1 (http://en.wikipedia.org/wiki/Maxwell's_equations), ref2 (http://hyperphysics.phy-astr.gsu.edu/hbase/electric/maxeq.html)
Ouabache
Jan6-06, 05:53 AM
Two Forms of Euler's Equation - commonly used in electrical engineering
Alternate form of Euler's Formula, see ref (http://mathworld.wolfram.com/EulerFormula.html)
Ouabache
Mar23-06, 07:47 PM
Start with Fourier's Law of Heat Conduction ref1 (http://www.efunda.com/formulae/heat_transfer/conduction/overview_cond.cfm)
\renewcommand{\vec}[1]{\mbox{\boldmath $ #1 $}}
\vec{Q} =-k \bar{\nabla} T
For this geometry (cylindrical tubing) by Fourier's Law, ref2 (http://www.engineersedge.com/heat_transfer/conduction_cylidrical_coor.htm)
Q=k A \left (\frac {\Delta T}{\Delta r} \right )
Heat Transfer Across Length of Cylindrical Tubing
\mbox {\Huge Q= $\frac {2 \pi k L (T_i-T_o)}{ln (\frac{r_o}{r_i}) }$ }
k - thermal conductivity of material [BTU/(hr-ft-deg F)]
L - length of tube (ft)
T_i - temperature along inside surface of tube (deg F)
T_o - temperature along outside surface of tube (deg F)
r_o - outside tube radius (ft)
r_i - inside tube radius (ft)
Q - heat transfer (BTU/hr)
Heat Flux - Heat Transfer Rate per Unit Area ref3 (http://www.tpub.com/content/doe/h1012v2/css/h1012v2_25.htm)
\bar{h} = \frac{\dot{m}c_p(T_{m,o}-T_{m,i})}{\pi D L \ \Delta T_{lm}} \ \ \ \ \ equ. (i)
\dot{m} flow rate of fluid (kg/s)
c_p specific heat at constant pressure [J/(kg-K)]
T_{m,i} mean temperature outside cyl. tube [deg C]
T_{m,o} mean temperature inside cyl. tube [deg C]
D diameter of cyl. tube [m.]
L length of cyl. tube [m.]
\Delta T_{lm} change in the log mean temperature [deg C]
\bar{h} ave. conv. heat transfer coef.[W/(m^2 - deg K)]