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Final Answers
© 2000-2008 Gérard P. Michon, Ph.D.

Differential Equations

Science is a differential equation.
Religion is a boundary condition.

 Alan Turing  (1912-1954)

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Related Links (Outside this Site)

SOS Math - Differential Equations
Ordinary Differential Equations & Partial Differential Equations  by  Eric Weisstein
 
Wikipedia:  Differential Equations   |   Ordinary Differential Equations   |   Cauchy-Lipschitz Theorem
 
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Differential Equations  (DE)


brentw ( Brent Watts of Hickory, NC. 2000-11-21)
How do I solve the following differential equations?
  1. [sin (xy) + xy cos (xy)] dx + [1 + x2 cos (xy)] dy = 0
  2. [4xy3 - 9y2 + 4xy2] dx + [3x2y2 -6xy + 2x2y] dy = 0
  3. (3x - y - 5) dx + (x - y + 1) dy = 0

1) For the first DE, what you have is clearly the differential of  [x sin(xy) + y]  so, the solution is:  [x sin(xy) + y] = constant.

2) The second DE has a singular solution (the straight line x=0). The general solution is obtained by noticing that the differential of [x4y3 - 3x3y2 + x4y2] is x2 times the given differential expression. The solutions to the DE are therefore either curves of equation [x4y3 - 3x3y2 + x4y2] =constant or "composite" curves made from such algebraic pieces and segments of the singular solution x=0 (joined at the points where they are tangent).

3) The last DE is a no-brainer, but a fairly annoying one. The general idea is to make a linear change of variables so that the variables "separate" easily. For example, you may use x=u+v and y=(u-v)Ö3, which means 4u=x+yÖ3 and 4y=x-yÖ3. Your DE then becomes something like (please check):

[2(Ö3+3)v + Ö3-5]du = [2(Ö3-3)u + Ö3+5]dv

If I did manipulate things correctly (please double check), this means that the solutions are the curves for which the following expression is constant:

[x - yÖ3 + 8/Ö3 - 6]3-Ö3 [x + yÖ3 - 8/Ö3+6]3+Ö3


Matthew A.  (Yahoo! 2002-07-21)   Singular Change of Variable
Solving the differential equation:   y dx   =   ( y ey - 2x )  dy

This example illustrates some of the issues which arise when a given differential equation reduces to a tame equation  (here a simple quadrature)  after a change of variable which presents some singularities...

If  y  is not zero (that's a big "if") we may replace  x  by the variable  u = x y.

du   =   y (y dx + 2x dy)

Multiplying both sides of the original equation by  y  turns it into:

du  =   y2 exp(y)  dy

Integration by parts then gives  u,  so we obtain the following expression:

x y2   =   (y2 - 2y + 2)  exp(y)  +  C

Any value of the "constant of integration"  C  can be used to obtain a solution over any domain in which  y  does not vanish...  However, for a well-behaved solution over a domain which crosses the line  y = 0,  we  must  use  C = -2.

x   =   [ (y2 -2y + 2) exp(y) - 2 ] / y2

It's only for this particular value of   C  that the function  x(y)  is smooth about  y = 0.  For small values of  y,  x(y)  is indeed infinitely smooth:

x   =   y/3 + y2/4 + y3/10 + y4/36 + y5/168 + ...

Now, what about  y  as a function of  x,  over the largest possible domain?  Well, the above function x(y) achieves a single  negative  minimum:

x   =   -A   =   -0.169998...       when   y  =   -1.45123...

For  x > -A,  the solution has two branches.  One corresponds to  y < -1.45123... and has an asymptote at  x = 0  (it does not extend to positive values of  x).

The other branch  (y > -1.45123...)  extends from  x = -A  to   and it goes through  x = 0,  y = 0  without the slightest glitch.


(2007-07-30)   Falling  vertically  in a fluid   (e.g., against air resistance).
The derivative of the downward speed is:   v'   =   g - ( 2 u v + v2 ) / l

In a vacuum, the  downward  speed  v  would increase at a rate  g  equal to the acceleration of gravity.  The resistive forces exerted by the medium  (e.g., air)  include a viscous resistance  (Stokes drag, proportional to  v )  and a pressure term  (also called  quadratic drag,  because it's proportional to the square of  v ).

With the notations introduced above,  2u  is the speed at which the quadratic drag becomes as large as the viscous term.  Loosely speaking,  2u  marks the middle of a transitional regime where the flow is no longer laminar, although the quadratic term of the turbulent regime is not yet dominant  (2u is sometimes dubbed "critical speed", although there's nothing critical about it).  The symbol  l  is a length which is inversely proportional to the magnitude of the pressure drag at high speeds.  Let's recast the above expression:

l dv/dt   =   ( lg + u2 )  -  ( u + v ) 2

Introducing a speed  w > u   defined by the relation  w2 = lg + u2 , we obtain:

l dv    =     [ w2 - (u+v)2 ]  dt Therefore :
2 w dt   =     2 w l dv     =     l dv    +    l dv
Vinculum Vinculum Vinculum
w2  -  ( u + v ) 2 w + u + v w - u - v

This is readily integrated from the beginning of the fall  (v = 0)  at time  t = 0 :

2 w t / l   =   Log ( [w+u+v] / [w-u-v] )  -  Log ( [w+u] / [w-u] )

Solving for  v  (HINT: take the exponentials of both sides)  we obtain:

v   =   ( w - u )  [  1 -   2 w   ]
Vinculum
(w-u) + (w+u)  exp ( 2wt / l )

By integration, this yields the height  h  traveled since the beginning of the fall:

h   =   ( w - u ) t  +  l Log [  w + u   +   w - u   exp ( - 2wt / l ) ]
Vinculum Vinculum
2 w 2 w

In practice, the exponential vanishes quickly and the dropped object travels at a uniform  terminal velocity  (w-u)  according to the following equation of motion:

h   =   (w-u) t - D

The distance  D = l [ Log 2 - Log (1+u/w) ]   can be interpreted either as a  time delay  or as a  correction in height  if you time the fall of an object dropped from an altitude  Z.  The actual duration of the fall will be the time it would have taken to travel the distance Z+D at a uniform speed equal to the terminal velocity.

Actual Physics :

The thrill of a closed solution to the above differential equation does not make that differential equation physically meaningful to begin with.  In fact, the two resistive terms in the equation correspond to two  separate  speed regimes.  It turns out that each term is small in the regime where the other is valid.  Therefore, adding up the two terms for  transitional  speeds is mathematically appealing.  Such a nice approximation may lack a firm physical basis, but I happen to like it.   ;-)

A resistive force proportional to speed occurs in the low-speed (viscous) regime where there's absolutely no turbulence in the wake of the moving object  (a so-called "laminar flow").  In that case, Sir George Stokes (1819-1903)  established a formula giving the resistive force  F  exerted on a  sphere  of radius  r  moving at speed  v  in a fluid of dynamic viscosity  h  (Stokes' Law, 1851):  Stokes

F   =   6p h r  v

On the other hand,  quadratic  drag  (proportional to  v 2 )  occurs in the turbulent regime normally associated with motion through air :

F   =   ½ r (C S)  v 2   =   ½ r (C p r 2 )  v 2

In this,  S = p r 2  is the cross-section of the object,  C  is a dimensionless  drag coefficient  (about 0.47 for a smooth sphere)  whereas  r  is the fluid's density.

Taking the above at face value for a sphere of mass  m  and  radius  r, we may reconcile both equations with our original notations:

l   =   2m / rCpr2       and       u   =   6h / rCr

For dry air at 20°C (1 atm)   r = 1.204 kg/m3   and   h = 1.808 10-5 Pa.s.  So, for a sphere  (C=0.47)  of radius  r = 1 mm, we obtain  u = 0.1917 m/s.

A sphere of density  d  has a mass  m = d 4pr3/3.  So  l  is proportional to  r:

l   =   r  (8d / 3rC)

With the above numbers and  d = 1000 kg/m3,  we obtain  l = 4.7 r.  For steel ball bearings  (d = 7850 kg/m3 )  we would have  l = 36.9 r. 

Poiseuille's Law   |   Stokes’ Law   |   Air Resistance   |   Terminal Velocity of a Skydiver

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