B. Reiser, REAL PROCESSING II - EXTREMAL PRINCIPLES OF IRREVERSIBLE THERMODYNAMICS, RELATIONS, GENERALIZATIONS AND TIME-DEPENDENCE, Physica. A, 253(1-4), 1998, pp. 223-246
We start presenting the extremal principles we will consider: The Stat
ement of Helmholtz 1868 and Rayleigh (SHR) 1913, generalized by Reiser
1996, the Statement of Kelvin (SK) 1849, the Principle of Minimal Ent
ropy Production (PME) of Prigogine 1947 for linear processes, that of
Prigogine and Glansdorff 1954 for non-linear processes and finally, th
e Principle of Maximal Entropy (MEF) of Jaynes, 1957. First we show th
e relation between SHR and SK. This is a particular example for the pr
operty of Irreversible Thermodynamics (TIP) to treat all kinds of move
ments of fluids, compounds or any type of energy under the engineering
term loss, or accurately spoken, entropy production. This possibility
to treat different physical effects in the same manner causes by its
simplification, considerable economical advantages of treating process
es in the frame of TIP. For example, whereas a balance like the moment
um balance (Navier-Stokes equation) has to distinguish between inertia
l, viscous or pressure effects, the PME treats the movements these eff
ects cause with one term, and no pressure coupling or nonlinearity is
enclosed. Then we generalize the SK from potential velocity fields to
general ones and show that it fits into the MEF. We continue with the
generalization of the SHR from 1996 to compressible and non-Newtonian
fluids. Further, we notice that these principles hold for rime-depende
nt processes. Therefore, the general fluid dynamical part of the PME 1
947 can be generalized from stationary to time-dependent (non-stationa
ry) processes. We;how that this is possible not only for velocity fiel
ds but also for scalar fields using as an example, the temperature in
the case of heat conduction. We see that scalar fields need a transfor
mation well known in mathematics. Comparing the PME 1954 with the comp
letely generalized SHR we see that it holds also for non-linear proces
ses. The same holds for the generalized SK. We close the consideration
of extremal principles with the formulation of a very general PME whi
ch may play the role of a main law of thermodynamics, the fourth one,
FML. We compare it with the Evolution Principle of Glansdorff and Prig
ogine 1964 and show how this may be generalized to time-dependent proc
esses too. The distinction between fixed- and free-process parameters
is particularly fruitful. The fixed ones are determined by balances an
d the free ones by the fourth main law (FML), In data processing this
separation allows for drastic simplification in the treatment of proce
sses: Not all process parameters have to be ''forced'' simultaneously
over the balances. They can be calculated separately. Finally, we cons
ider an application of the PME to the improvement of the performance o
f an evaporator. This improvement is considerable and stands for the m
eaning of TIP-applications to other ranges of process engineering, in
particular to complicated processes: e.g, those with phase changes. (C
) 1998 Elsevier Science B.V. All rights reserved.