1549301742-The_Theory_of_Difference_Schemes__Samarskii

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Conservative schemes^151

conservation laws (of heat, mass, momentun1, energy, etc.). Usually the
derivation of a differential equation of mathematical physics is on an in-
tegral relation (a balance equation) which expresses such a conservation
law for a small volume. Letting the volume to zero and assuming that the
derivatives involved in the balance equation are continuous, one can write
down the appropriate differential equation.
From a physical point of view, the finite difference method is mostly
based based on the further replacement of a continuous medium by its
discrete model. Adopting those ideas, it is natural to require that the
principal characteristics of a physical process should be in full force. Such
characteristics are certainly conservation laws. Difference schemes, which
express various conservation laws on grids, are said to be conservative or
divergent. For conservative schemes the relevant conservative laws in the
entire grid domain (integral conservative laws) do follow as an algebraic
corollary to difference equations.
In this view, it see111s reasonable to construct conservative difference
sche111es with the aid of balance equations for an elementary volume (cell) of
a grid domain. Integrals and derivatives involved in these equations should
be replaced by approximate difference expressions, thereby completing the
design of a homogeneous difference scheme. The way of obtaining homoge-
neous difference schemes is called the integro-interpolational method
or balance method.
In what follows the illustration of this method is concerned with equa-
tion ( 1) from (Section 1) capable of describing the stationary distribution
of temperature over a homogeneous bar 0 < x < 1. The equation of the
heat balance can be written on the segment xi_ 112 < x < xi+ 1 ; 2 as

xi+1/2 xi+1/2
( 11) wi-1/2 - wi+1/2 + j f(x) dx = j q(x) u(x) dx,
Xi-1/2 Xi-1/2
w -- -k u' '

where w(x) is the heat flow, q(x) u(x) is the capacity of heat sinks (sources
for q < 0) proportional to the temperature and J(x) is the distribution
density of external heat sources (sinks).
The existence of a heat sink owes a debt to the heat exchange with the
external environment on the lateral surface of the bar. The quantity wi 112
is equal to the amount of heat being supplied to the segment X;
112 < x <
xi+ 1 ; 2 through the cross-section x = xi_ 112 , while wi+ 1 ; 2 refers in a similar
fashion to the heat transfer from this segment through the cut x = X;+ 1 ; 2.
The third member on the left-hand side of ( 11) reflects the amount of

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