1

1
DYNAMIC APPROACH TO THERMODYNAMIC SIMULATION OF CHEMICAL SYSTEMS:
FROM TRUE EQUILIBRIUM TO TRUE CHAOS.
B. Zilbergleyt,
System Dynamics Research Foundation, Chicago
E

mail:
livent@ameritech.net
ABSTRACT.
The pa
per presents new model of equilibrium in open chemical systems suggesting linear
dependence of the reaction shift from true equilibrium on the external thermodynamic force. Basic equation of
the model includes traditional logarithmic term and non

tradition
al parabolic term. Behavior of open system is
defined by relative contributions of both terms. If classical logarithmic term prevails open system can be in
equilibrium. Increased weight of non

classical
chaotic
term leads open system to bifurcations and ch
aos. Area
of open equilibrium serves as a water shed between true equilibrium and bifurcations and eventual chaos. In
simple isolated equilibrium the chaotic term equals to zero turning the equation to traditional form of constant
equation. Formally this t
erm matches excessive thermodynamic function showing linear relationship between
reaction extent in open equilibrium and logarithm of coefficient of thermodynamic activity. In form of chaotic
term it reveals new behavioral features of open systems while me
thod of coefficients of thermodynamic
activities hides them to keep open system disguised as isolated entity. Discovered relationship prompts us to
use the coefficient of linearity in combination with reaction shift rather than activity coefficients. This
coefficient in open equilibrium can be calculated in a simple way using basic equation and reaction shift as
independent variable. Numerical data obtained by various simulation techniques have proved premise of the
new theory and following from it method o
f chemical dynamics.
INTRODUCTION: BACK TO CHEMICAL DYNAMICS.
Nowadays we know that chemical self

organization happens in a vaguely defined area “far

from

equilibrium”[1], while classical thermodynamics defines what is frozen at the point of true equilibr
ium. What
occurs in between?
“True”, or “internal” thermodynamic equilibrium is defined by current thermodynamic paradigm only for
isolated systems. That’s why applications to real systems often lead to severe misinterpretation of their
status, bringing
approximate rather than precise results. A few questions arise in this relation. Is it possible to
expand the idea of thermodynamic equilibrium to open systems? How to describe and simulate open
equilibrium in chemical systems? Is there any relationship be
tween deviation of a chemical system from “true”
equilibrium and parameters of its non

ideality?
Current paradigm of chemical thermodynamics handles open chemical systems employing coefficients of
thermodynamics activities. The coefficients as well as th
e whole concept of equilibrium, based on Guldberg

Waage’s equation, may be derived from the probability theory [2]. Indeed, chemical system with only one
type of collision is a simple chemical system: one type of collision
–
one reaction
–
one outcome, and
chance
of the reaction to happen is
proportional to P(A)

probability of reactants to collide, equal to the particles
mole fractions product. In complex systems with multiple interactions, according to the Bayes’ theorem,
instead of
P(A) we consider P(A/
B)
–
conditional probability
of collision A given another collision, B, took
place. The ratio
=P(A/B)/P(A) defines a coefficient, currently known as coefficient of thermodynamic
activity.
Regardless of the initial idea, introduction of
coefficients of thermodynamic activity
was and still is a
great contribution to chemical thermodynamics
mainly be
cause it allowed scientists to keep expressions for
G and constant equation unchanged still holding open systems in a mask of isolated entities. The name of
the
Law of Active Masses
became more clear

may be considered a fraction of a substance availab
le to
participate in chemical reaction. Later on value of
was tied to excessive thermodynamic functions though
experiment is often the best way to obtain it.
The values to be introduced and discussed in this paper are sensitive to isolation or openness o
f the systems
where the chemical processes are to run. An isolated system will be referred to as
system
with possible true
thermodynamic equilibrium.
Simple chemical system
allows only one chemical reaction to run towards true
thermodynamic equilibrium. Th
ermodynamic state of such a system is defined by two thermodynamic (e.g., P,
T) and one chemical (reaction coordinate
parameters. For the sake of clearness, simplicity and to keep it
closer to reality, open system will be considered also allowing for one chemical reaction to run thus being a
simple
subsystem
–
a part of bigger and more complex chemical system. The syst
em contains a set of similar
1

2
entities as subsystems and constituted by chemical (or thermodynamic) interaction between them. For
example, in some cases it is very convenient if reaction of formation of one chemical substance from elements
runs in each subs
ystem. This way number of subsystems will equal to the number of chemical species in the
system. We define thermodynamic equilibrium in open system as
open equilibrium
. It is the central idea of the
present paper, and we will get its basic equations, show
where it leads the open system and how to bring the
ideas to numbers.
To do so we will use currently almost neglected method de Donder that introduced thermodynamic affinity
interpreting it as a thermodynamic force and considering the reaction extent a “
chemical distance” [2]. It is
more convenient to use redefined reaction coordinate d
j
=dn
kj
/
kj
, instead of d
j
=dn
kj
/
kj
by de Donder, or
reaction extent
j
=
n
kj
/
kj
in increments. Value of
n
kj
equals to amount of moles, consumed or appeared in j

reaction between its two arbitrary states, one of them may be the initial state. The
ij
value equals to a number
of moles of k

component, consumed or appeared in an
isolated
j

reaction on its way from initial state to true
equilibrium and may be considered
a thermodynamic equivalent of chemical transformation
. This value is
unambiguously rela
ted to standard change of free Gibbs’ energy or equilibrium constant of reaction and
represents natural and the only result of thermodynamic simulation of the reaction equilibrium. Above
redefined value of the reaction extent remains the same being calcula
ted for any component of a simple
chemical reaction; the only (and easily achievable by appropriate choice of the basis of the chemical system)
condition for this is that each chemical element is involved in only one substance on each side of the reaction
equation like in reactions of formation from elements. Now, in our definition
j
is a dimensionless chemical
distance (“cd”) between initial and running states of j

reaction, 0
≤
j
≤
1, and thermodynamic affinity A
=
(
G/
)
p,T
turns into a classical force by definition, customary in physics and related sciences.
Chemical reaction
in
isolated system
is driven only by internal force (eugenaffinity, A
ij
). True thermodynamic
equilibrium occurs at A
´
ij
= 0 and at this point
´
j
= 1. Reactions in
open system
are driven by both
internal
and
external
(A
ej
) forces. The external force orig
inates from chemical or, in general, thermodynamic (also due
to heat exchange, pressure, etc., affecting thermodynamic parameters of its state) interaction of the open
system with its environment. Linear constitutional equations of non

equilibrium thermod
ynamics at zero flow
give us a condition of open equilibrium with resultant affinity
A*
ij
+
ie
A*
ej
= 0, (1)
where
ie
= a
ii
/a
ie
is a ratio of the Onsager/Kasimir coefficients [3]. The accent mark and asterisk relate values
to isolated (“true”) and open equilibrium corres
pondingly, and indices ‘i’ and ‘e’ define internal and external
variables and functions correspondingly.
In this work we will use only one assumption which in fact slightly extends the hypothesis of linearity. Given a
relation between the reaction shift f
rom equilibrium
j
=1
j
and external thermodynamic force causing this
shift, we will suppose
at the first approximation that
the reaction shift in the vicinity of true thermodynamic
equilibrium
is linearly related to the shifting force
j
=
ie
A
ej
.
(2)
Recalling that A
i
=
(
G
i
/
i
), or A
i
=
(
G
i
/
i
) and substituting (2) into (1), we will get an intermediate
expression
–
(
G*
ij
/
*
j
) + (
ie
/
ie
)
*
j
= 0.
(3)
After a simple transformation, retaining in writing only
j
for
j
and
j
for
j
we turn it into
G*
ij
+ b
ie
*
j
*
j
= 0, (4)
where b
ie
=
ie
/
ie
). As usually,
G*
ij
=
G
0
ij
+ RTln
*
j
(
,
*
j
) , and corresponding constant equation is
RTlnK
j
+ RTln
*
j
(
,
*
j
) + b
ie
*
j
*
j
= 0, (5)
w
here
*
j
(
,
*
j
) is the product of mole fractions in open equilibrium expressed via j

reaction extent. Please
notice that equilibrium constant K
j
=
'
j
(
,
).
Obviously product
*
j
*
j
is dimensionless, therefore b
ie
has dimension of energy. To bring (5
) to more
symmetric form we introduce a new value

the “alternative” temperature of the open system
T
a
= b
ie
/ R, (6)
R is universal gas constant. The value of T
a
is introduced
in this work for convenience and symmetry; we
cannot clearly explain its physical meaning at this moment. The logarithmic term contains traditional
thermodynamic temperature T
t
, and (5) turns to
RT
t
ln
`
j
+ RT
t
ln
*
j
+ RT
a
*
j
*
j
= 0.
Now, dividing (7) by (
RT
t
), and denoting
= T
a
/T
t
, we transform equation (7) into
ln [
`
kj
,1)/
kj
,
*
j
)]
j
*
j
*
j
= 0.
(8)
___________________________________________________________________________________
___
“
Vicinity
” in this case is certainly not less vague than “
far

from

equilibrium
”. Some discussion see below.
1

3
So,
as so
on as chemical system becomes open, appropriate constant equation includes a non

linear, non

classical term originated due to system’s interaction with its environment
.
What opens up immediately is a similarity between the non

classical term of (5) and the
well known product
r
⠱
x) from so called
logistic map
[4], which is one of the most convincing equations leading to bifurcations
and chaos. We refer alternative temperature to as
chaotic temperature
T
ch
and
j
as
reduced chaotic
temperature
.
Being div
ided by
*
j
, this equation expresses linearity between the thermodynamic force and reaction shift
{ln [
`
kj
,1)/
kj
,
*
j
)]}/
*
j
=
j
*
j
, (9)
both parts of it are new expressions for the th
ermodynamic force. Equality (9) contains condition of open
equilibrium as balance of internal and external thermodynamic forces. Equation (8) can be written in more
general form as
*
=
*
(10)
It is easy to see that in case of isolated system
*=
external thermodynamic force equals to zero, and (8)
turns to the normal constant equation. For better understanding of internal relations between (9) and constant
equation one sh
ould recall once again that
serving as a parameter in
(10), is the only output from the
solution to constant equation (because
n`
n
0
, where right side contains equilibrium and initial mole
amounts).
INVESTIGATION OF THE FORCE

SHIFT RELATIONSH
IP.
First, consider the force expression from equation (9). Its numerator is a logarithm of a combination of molar
fraction products for a given stoichiometric equation. The expression under the logarithm is the molar fraction
product for ideal system div
ided by the same product where
kj
replaced by
*
j
kj
due to the system’s shift
from “true” equilibrium. Table 1 represents expressions for thermodynamic forces of some simple chemical
reactions with initial amounts of reactants A and B both equal to one mole. Graphs of the reaction shi
fts vs
thermodynamic forces are shown at Fig.1. One can see visually distinctive linearity (actually, quasi

linearity)
on shift

force curves. Extent of the linearity region depends on the
value.
Going down to real objects, consider a model system contai
ning a double oxide MeO
RO and an independent
reactant I (for instance, sulfur) such that I reacts only with MeO
, while
RO restricts reaction ability of MeO
Table 1.
Thermodynamic forces {ln[
`
kj
,1)/
kj
,
*
j
)]}/
(eq. 8) for some simple chemi
cal reactions.
Initial amounts of reactants are taken equal to 1 mole and initial products to zero for simplicity.
Reaction equation.
Thermodynamic force
A + B = C
{ln {(1/
⠲
)/(
⥝嬨)
)/(1
⥝
2
}}/
†
A+B=C
{ln{(1/
⠱
)/(1
嬨
)/(1
⥝
2
}}/
A+B=C
{ln{(1/
嬨
3
[(1
4
}}/
†††
††††
Fig.1.Shiftofsomesimplechemiclrectionsfromtrueequilibr
ium
vs. shifting force F, kJ/m
∙
cd. Reactions,
left to right, values of
in brackets(curves follow right to left) : A+B=AB (
, 0.9), A+2B=AB
2
(
2A+2B=A
2
B
2
(
. Also, linear areas on the curves give an
e
stimation of how far the “vicinity of equilibrium” extents.
1

4
and frees in the reaction as far as MeO
is consumed. Two competing processes are in equilibrium in the
isolated system

decomposition of MeO
RO, or restricting reaction: MeO
RO = MeO + RO, and
leading
reaction: MeO + I =
*
L
, the right side in the last case represents a sum of products. Resulting reaction in the
system obviously is MeO
RO + I =
*
L
+ R.
To obtain numbers for real species, we used thermodynamic simulation (HSC Chemistry for Windo
ws) in the
model set of substances. The Is were S, C, H
2
, and MeO
RO were double oxides with symbol Me standing for
Co, Ni, Fe, Sr, Ca, Pb and Mn. As restricting parts
RO were used oxides of Si, Ti, Cr, and some others. Chosen
double oxides had relatively
high negative standard change of Gibbs’ potential to provide negligible
dissociation in absence of I. For more details see [5]. Some of the results for reactions (MeO
RO
+S) are shown
on Fig.2. In this group value of (
G
0
C
/
*
L
)
I
plays role of external thermodynamic force regarding the
(MeO+S) reaction.
The most important is the fact that in both cases the data, showing the reality of linear relationship, have been
received using exclusively current formalism of c
hemical equilibrium where no such kind of relationship was
ever assumed. It is quite obvious that linear dependence took place in some cases up to essential deviations
from equilibrium. We call the method, described in the present work (also including orig
inal de Donder’s
approach), a
force

shift method
for explicit usage of chemical forces, originally introduced as thermodynamic
affinities, or a
method of chemical dynamics (MCD)
. Results shown on Fig.1 and Fig.2 prove the premises
and some conclusions of t
he theory.
Fig.2. Reaction shift
*
vs. force F=
G
0
MeO
RO
/
*, kJ/m
∙
cd, 298.15K, direct thermodynamic simulation.
Points on the graphs correspond to various
RO. One can see a
delay along x

axis for CaO
RO.
Within current paradigm of chemical thermodynamics, constant equation for non

ideal system with
k
1 is
G
0
j
=
RT
t
ln
*
k
RT
t
ln
*x
k
,
and x
k
are molar fracti
ons, power values are omitted for simplicity. The non

linear term of the equation (8) also
belongs to a non

ideal system, and comparison of (8) and (15) leads to following equality in open equilibrium
with precision of the sign
j
*
j
ln
*
k
)
/
*
j
.
(16)
If
*
k
<1, the minus sign should be placed on the left side. This result is quite understandable. For instance,
in case of MeO
RO the chemical bond between MeO and RO reduces
reaction a
ctivity
of MeO; the same
result will be obtained for reaction (MeO + I) in absence of RO and with reduced coefficient of
thermodynamic
activity
of MeO. Now, to avoid complexity and using only one common component MeO
in both
subsystems, the relationship b
etween the shift of the (MeO +I) reaction and activity coefficient of MeO
is
very simple
* = (1/
)
(ln
*)/
*],
(17)
where
*,
and
* are related to the
(MeO +I) reaction, and
(ln
*)/
*] is external thermodynamic force
acting against it (divided by RT
t
).
This expression for th
e force as well as the total equation
(17)
are new
.
This equation connects values from the MCD with traditional values of chemical thermodynamics. Yet again,
at
*
L
= 0 we have immediately
*=1, and vice versa, a
correlation, providing an explicit and insta
nt
transition between open and isolated systems.
In case of multiple interactions one should expect additivity of
the shift increments, caused by interaction with different reaction subsystems, which follows the additivity of
appropriate logarithms of act
ivity coefficients. This is also proven by simulation.
Data for Fig. 3 were obtained using two different methods of thermodynamic simulation. I

simulation relates to
an isolated (MeO
RO+I) system with real MeO and RO and
MeO
= 1 in all cases. In O

simulation a
_______________________________________________________________________________
1

5
The numerator is free energy of formation of double oxides MeO
RO
from oxides MeO and RO.
combination of MeO+Y
2
O
3
+I represented
the model of open system where
RO was excluded and replaced by
yttrium oxide, neutral to MeO and I to keep the same total amount of moles in the system as in I

simulation
and avoid interaction between MeO and RO, which role was played by Y
2
O
3
. Binding of
MeO into double
compounds with RO, resulting in reduced reaction ability of MeO was simulated varying
. I

simulation
provided a relationship in corresponding rows of the
*
L

* values, and O

simulation

with
*
L

G
0
MeO
RO
Fig. 3.
*
vs. (

ln
*) (I

simulation, x) and vs. (
G
0
MeO
RO
/
*) (O

simulation, o), (MeO
R
+S). PbO
and
CoO
at 298K, SrO
at 798. Curve for SrO
shows light delay along the x

axis.
correspondence. Standard change of Gibbs’ potential
G
0
MeO
RO
, determining strength of the MeO
RO bond,
was considered an excessive thermodynamic function to
the reaction (MeO+I).
We have calculated some numeric
values from the data used for plotting Fig.2, they are shown in Table 2. It
is worthy to mention that the range of activity coefficients, usable in equilibrium calculations, seems to be
extendible do
wn to unusually low powers (see Fig.1).
Strong relation between reaction shifts and activity coefficients means automatically strong relation between
shifts and excessive thermodynamic functions, or external thermodynamic forces. Along with standard change
of Gibbs’ potential we also tried two others
–
the Q
which was calculated by equation (17) with
*
, used in the
O

simulation, and another,
G*
MeO
RO
,
found as a difference between
G
0
MeO
RO
and equilibrium value of
RT
t
ln
*x
k
. Referring to the same
*, all three should be equal or close in values. Almost ideal match,
illustrating this idea, was foun
d in the CoO
RO

S system and is shown on Fig.5. In other systems all three
were less but still are close enough. Analysis of the values, which may be used as possible excessive
functions, shows that the open equilibrium may be defined using both external
(like
G
0
MeO
RO
) and internal
(the bound affinity, see [4]) values as well as, say, a neutral, or general value like a function calculated by (17)
at given activity coefficient.
Table 2.
Reduced temperatures, standard deviations and coefficients of determ
ination between
*
and (
ln
*) in
some MeO
RO

S systems. Initial reactants ratio S/MeO = 0.1.
CoO*RO
SrO*RO
PbO*RO
T
t
, K
298.15
798.15
298.15
4.
.54
.9
†
Stndrddevition%
8.99
.99
.8
†
Coefficientofdeter
mintion
.98
.99
.97
nprinciplellthreemybeusedtoclculteorevlute
L
. This allows us to reword more explicitly the
problem set in the beginning of this work and explain the alternative temperature more clear. It is easy to see
that equ
ation (17) represents another form of the shift

force linearity.
Recalling that
= (T
ch
/T
t
), one can receive
* = [1/(RT
ch
)]
•
(Q
E
/
*), (18)
where Q
E
is a general symbol for excessive thermod
ynamic function.
It means that the shifting force is
unambiguously related to the excessive function, and the alternative temperature is just inverse to the
1

6
coefficient of proportionality between the force and the shift it causes. The product RT
ch
has dime
nsion of
energy while
and
are dimensionless.
To compare values of
received with different methods
we put them together in one Table 3. Abbreviations in
the table means: R

simulation
–
thermodynamic simulation of homologous series of reactions with
MeO
RO,
(ElRea)

simula
tion
–
abstract simulation of elemental reactions with corresponding reaction equation and
varied
, and
simulation
stands for thermodynamic simulation with artificially varied coefficients of
thermodynamic activity. In some cases (like in reaction 2CoO+
S=2Co+SO2 at 298K) results match very well,
but in some cases, like in the example below, the match is not very good.
All results depend upon precision of input thermochemical information used to calculate equilibrium
composition. It seems that in case of (ElRea)
–
simulation this dependence is less expressed, and this method
may be more preferable.
Table 3.
Red
uced chaotic temperatures and average deviations. Reactions MeO+H2=Me+H2, 973K,
initial MeO:H2=1:1.
MeO
*
scope

simultion
Ele

simultion
simultion
Avedev%%
Avedev%%
Avedev%%
Ni
.9
.4
4.8
1.
18.9
4
.7
19.77
1.9
Cd
.88
††
縠.
19.
.1
15.
4
1.5
14.9
1.74
Co
.85
†
.4

.5
17.
.1
1.8
8
.9
1.8
1.75
CHEMICAL ANALOG OF THE HOOKE’S LAW.
Linearity of the shift vs. the force up to certain yield point and then sharp deviation from linearity
(see Figs 1
and 4) bring to mind an idea that there should exist a kind of chemical analog to the Hooke’s law, well known
in mechanics of materials. We have investigated about a hundred of reactions between double oxides with
essential negative values of s
tandard changes of Gibbs’ energy of formation and various reductants like S,
H2,
Fig.4. Reaction shifts vs. external thermodynamic forces for reactions of 18 double
oxides with sulfur, Gibbs’ energies in kJ/(mole*K).
CO. In all cases relationship was similar. In addition to the mentioned pictures, typical reaction shifts
distribution in open equilibrium vs. external thermodynamic forces for reactions MeO
RO+S at 298K is shown
in Fig.4.
According to theory of elasticity
, deformation of a material, which in one

dimensional case equals to the ratio
of elongation to the initial length of sample, x/L, and tension in the deformed material, which is equal to the
ratio of deforming force to the area of the perpendicular to the
force section, are related as
(x/L) = (1/E)(F/S), (19)
where E
Young’s coefficient of elasticity.
1

7
In our case, replacing tension by the thermodynamic force, which has a dimension of force strength (because
it is a ratio of free energy change to the reaction extent, that is to “chemical distance” between initial and
open

equilibrium states), juxtaposing deformation to the reaction shift
*, and “true” equilibrium reaction
extent
= 1 to the initial length of the sample, one can easily get
* = (1/
)F,
(20)
Comparison between (17) and (20) unambiguously shows similarity between the reduced chaotic temperature
and Young’s module E. As far as reaction shift
* stays within the linearity region, elimination of
thermodynamic force will bring the system
back to the state of isolated, “true” equilibrium, reaction shift turns
to zero. Reduced chaotic temperature plays role of the elasticity module, and the yield point corresponds to
the proportionality limit. In the mechanical law elastic potential, or pot
ential energy of elastic deformation is a
quadratic function of deformation. The expression for the change of free Gibbs’ energy in open system it is
also a quadratic function of the reaction shift from equilibrium because
It is quite obvious that
positive value of the reaction shift corresponds to “compression” while extension is analogous to the
situation with the negative reaction shift value (
1). Suggestions of this chapter may lead to a new
thermodynamic
approach to chemical hysteresis.
CHAOS OUT OF ORDER.
Previous parts of this paper were related to equilibrium states of open chemical systems while current part is
intended rather to analyze the features of basic equation. Let’s put down equation (8)
in a short form
ln (
`/
*)
*
*
= 0. (
2
1)
As it is shown on Fig.5, open equilibrium occurs at the crossing of the logarithmic term as function of
j
and
chaotic term
j
j
j
.
The origin of the term “chaotic
” in application to some values of this work was explained above with regard to
logistic map, which in form o equation looks like
x
n+1
x
n
(1
x
n
)
= 0
. (22)
Values of
*
j
in (21) and x
n
in (22) are supposed to stay within the range (0,1). Due to intensive study of the
chaotic processes for more than two decades, properties of (22) are well known while equation (21), to the best
of our knowledge, has never been investigated from this point
of view. At the same time, very interesting
features of open chemical systems may be discovered through its study.
Value of
as well as

value define the fate of iterations, which are important not only for calculating algorithm
but also for understanding and control processes in complex chemical systems. To refresh reader’s memory,
we will give a very brief summary of key po
ints related to properties of the logistic equation following [5].
Condition 0<
<4 and initial choice x
0
(0,1) keeps all x values within the same range in the run of iterations. If
<1, the only steady solution is x=0. At
3
1
first bifurcation occurs and
solutions to equation (22) split with
period 2. At
3.5 next bifurcation takes place turning the period to 4, at
3.54 period doubles again and
becomes equal to 8, and so forth. Further increase of
beyond ~ 3.5699… leads to non

repeating sequence of
nu
mbers referred to as
chaotic
.
It is obvious that in case of more complicated equation (21) (we will refer it to as OpEq equation or
log

logistic
map
), the solutions behavior will depend upon relative contributions of both terms
–
classical logarithmic,
wh
ich tends toward classical pattern of isolated “true” thermodynamic equilibrium, and non

classical chaotic,
leading the open chemical system to bifurcations and chaos. This paper presents results of
preliminary
investigation of the OpEq equation using as e
xample elemental reaction A+B=C under the influence of these
two powers.
Classical paradigm of chemical thermodynamics admits only one state of equilibrium (Zel’dovich’s theorem,
[7]). This statement is valid only for simple isolated chemical system. Ther
e are two possibilities in case of
open equilibrium before bifurcations and then following chaos occur. Equation (21) has 2 solutions as
minimum
–
trivial at
=0, where both curves have one joint point (as with
=1 on Fig.5), and also non

trivial
with
>0
which represents namely open equilibrium and has at least one crossing point with the second term
(upper parabola). If such point exists then open equilibrium has a non

trivial solution. Both logarithmic and
chaotic functions are continuous, differentiable
and monotonous, and non

trivial solution of open equilibrium
exists if derivative of the logarithmic curve is less than derivative of the chaotic curve in the initial point
=0
d
ln(
`/
*)/
d
<
d
(
)/
d
(23)
Minimal value of
, providing existence of non

trivial solution, can be easily received from (8). Its right side
equals merely to
, while left side, taking into account that
`=K, gives a product (1/K)
d
*/
d
, and
(1/K)
d
*/
d
.
(24)
Minimal value of
is totally defined by K, or the thermodynamic equivalent of chemical transformation
, and
reaction equation (which defines expression for
*). Though numbers used to plot graph on Fig.
5 are tajken
for example, the result is quite simple

if condition (24) is reversely satisfied, the
logarithmic term essentially
prevails and open system still has only one attractor

true thermodynamic equilibrium.
All states below curve
1

8
(1) in Fig.8 sa
tisfy condition (24) and solution is
=0.
If a non

trivial solution to (21) exists, possibility to find
bifurcations due to the chaotic term becomes real.
In one

approach we investigated iterative behavior of the basic equation solutions at fixed values
of
just to
grasp the picture in general. Typical iterative graphs are shown on Fig.6. Period n means n possible solutions.
Fig.7 presents diagram of states of open chemical system with reaction A+B=C.
This
diagram
perhaps is the
most important result of
this work. One can distinctively see 3 areas on the diagram
–
true equilibrium
where
Fig.5. Logarithmic and chaotic terms of the basic OpEq equation as functions of
the shift
between open and true thermodynamic equilibrium
*
j
.
curves are laying immediately on abscissa and all the
way long
have
=0, open equilibrium
from the points of
>0
to the split points, and
bifurcations after
the split points. At the tail

ends of the spli
t curves
period
doubles.
Fig.6. Bifurcation of solutions to the basic equation. Reaction A+B=C,
=0.1.
Abscissa
–
number of iterations.
Impor
tant is the fact that open system still stays in open equilibrium up to essential values of reduced chaotic
temperatures, and further increase of
must occur to move open system up to the split point.
Fig.7. State diagram of the open chemical system, reaction A+B=C,
corresponding
values: 1
0.1, 2
0.5, 3
–
0.7.
Table 3.
Relation between parameter
and
on two equilibrium limits, TTDE
–
true equilibrium, OpEq
–
open
eq
uilibrium, reaction A+B=C, initial reactant amounts equal to unity.
(
)/T
TTE
pEq
1

9
0.1
0.24
12.06
1.2
7.4
0.3
1.04

0.33
1.6
8.6
0.5
3.00

9.13
2.7
10.3
0.7
10.11

19.24
5.2
12.5
0.9
99.00

38.21
13.1
18.5
Fig. 7 exemplifies explicitly the
influence of the parameter
a
symbol of the reaction “classical
strength”. Numerical data is placed in Table 3 (initial amounts of reactants moles were equal to unity).
Fig.8.
Thresholds of trivial solution (upper limit to true equilibrium, 1) and first bifurcation (upper limit to open
equilibrium or equilibrium at all, 2) (with precision of
~ +/

0.05): a) vs. TD

equivalent (points on
x

axis with numbers 1 to 5 correspond to
=0.1, 0.3, 05, 0.7, 0.9), and b) vs.
G/T, reaction A+B=C.
We have placed in Table 3 and on Fig.8b also more habitual values of equilibrium constant K and reduced
changes of Gibbs’ free energy
G/T
t
along with values of
. Chaotic temperature in all cas
es as well as change
of free Gibbs’ energy is reduced by thermodynamic temperature, and both are counted in values per Kelvin’s
degree.
Due to above mentioned similarity with the Hooke's law, value of
beyond the yield point is always different
than below
it. This feature may influence the results. One should also account coordinate
y
of the yield point
itself, this brings the number of independent parameters to at least 4. To investigate the case with two values
of
the
calculation program was designed
so that reaction shift was iterated first with initial value of
corresponding to the left, ascending part of the graph on Fig.2. As soon as running value of
hit the yield
point, iterations automatically continued with second value of
always bigger th
an the first as it was already
mentioned above. It occurred that if
y
was within very reasonable limits (0.3
0.7; the values found earlier for
real systems) second
played major role in the system behavior. The most unexpected discovery was that the
tw
o

calculation results didn’t have a big difference with one

approach

region of trivial solution stayed
almost untouched, and no matter how big were the values of the first
(if less than thresholds in Table 1),
bifurcations eventually occurred when
second
reached about the same bifurcation threshold numbers as the
only
in one

model. Because we couldn’t find any really distinguishable points for the two

model, our
major conclusion is that it features the same threshold values as one

approach
.
We would like to focus reader’s attention once again on Fig.7 and Fig.8 containing graphical images of the
most important things discovered in quite simple reaction by the new theory. Area below curve 1 in Fig.8
corresponds to true thermodynamic equilibr
ium (
=0) though value of
already isn’t zero. Area between
curves 1 and 2 corresponds to open equilibria (0<
where non

trivial solutions to (21) reside
rea above
curve 2 corresponds to bifurcations and no equilibrium at all. Therefore, zone of open
equilibria with non

zero
shifts separates true equilibrium and chaos, or classical and non

classical areas, serving as a water shed
between regular and strange attractors. It is noteworthy and quite natural that the more negative is standard
change of fre
e Gibbs’ energy of reaction the higher are limit values of reduced chaotic temperatures.
A subtitle of this part of the paper could be “
How simple is simple reaction A+B=C?
”. As it follows from
here presented preliminary results, this reaction ceases to be
simple as soon as it runs in open chemical
system.
PRACTICAL APPLICATIONS.
With current methods in chemical thermodynamics, we have to know appropriate coefficients of
thermodynamic activity in order to simulate and compute equilibrium composition of m
ost complex chemical
systems. Their numeric values are not always available, and it is usually very expensive to get them when we
are in need. MCD offers an easier and involving much less efforts way to run that kind of simulation. Indeed,
this new theory
interprets equilibrium of complex chemical system as truly internal equilibrium constituted by
1

10
a set of subsystems’ equilibria, explicitly defined by appropriate set of basic equations. Now, having the
kj
value from solution for the isolated state and
j
as a characteristic for subsystem response to external
thermodynamic perturbation (as it was above described in details), we can get equation (8) in form (21)
containing only variable
and parameter
.
Current methods of simulation of complex equilibri
um use the constant equations (or equivalent to it
minimization Gibbs’ potential of the system) in the same form as if subsystems are isolated, occasionally using
not always available coefficients of thermodynamic activity. In most cases their joint soluti
on actually only
restricts consuming the common participants, watching material balance within the system and playing role of
accountant. Application of current methods to real systems leads to some definite errors in simulation results
originated due to m
isinterpretation of their status [6]. Method of Chemical Dynamics assumes states of
subsystems as open equilibria within complex equilibrium and should give more correct numerical output.
A principal feature of application following from our method consis
ts in usage of reaction shift
*
j
(as the
system’s response to external impact) multiplied by coefficient
proportionality rather than activity coefficient
k
. Providing with an easy way to obtain value of
j
in open equilibria within minutes, MCD brings ne
w
opportunities into analysis and simulation of complex chemical systems.
Another new in principle opportunity consists in analysis of equilibrium and non

equilibrium areas of
solutions to the basic equation of the theory. This allows us to evaluate critic
al values of external impact
(values of
to keep open system within desirable areas.
DISCUSSION.
The new basic equation derived in this work links equilibrium (corresponding to isolated systems) and non

equilibrium thermodynamics (making sense in open
systems), and may be rewritten more generally as
Gj
G
0
j
+ RT
t
f
t
(
*
j
RT
ch
f
ch
(
*
j
.
The method treats true, isolated thermodynamic equilibrium of a system as a reference state for its open
equi
librium when system becomes a part of a bigger system. This reference state is memorized in
kj
. Such an
approach matches well the interpretation of equilibrium at zero control parameters (area below line 1 in Fig.8)
as origin of the chaosity scale (the S

theorem, [8]).
Based on a very simple and quite natural assumption,
t
he
basic equation of the present work naturally and smoothly drags non

linearity into thermodynamics of
open systems thus bridging a gap between classical and non

classical thermodynamics
. Offered in this
paper theory represents new, unified thermodynamics of chemical equilibria fitting open systems as well as
isolated chemical systems as a particular case.
Going down to the results, one can see that system behavior is essentially affected
by parameter
. Depending
upon the value of standard change of Gibbs’ energy (or
), system still will not deviate from true, classical
thermodynamic equilibrium if external impact doesn’t bring the ratio T
ch
/T
t
beyond a certain value. The
bifurcation thr
eshold features the same dependency. We can strongly declare
that evolution of open
chemical system from thermodynamic “dead” order through bifurcations to “vivid” chaos, i.e. its transition
from kingdom of thermal energy to the point where it gives up to
external power, is driven by ratio between
chaotic and thermodynamic temperatures.
We should confess so far that our actual understanding of physical meaning of the chaotic temperature and
how to estimate it independently is far from clarity. We know for
sure that in open equilibrium value of
reduced chaotic temperature
can be easily found for any equilibrium value of reaction extent
* directly from
the basic equation (e.g., 21) and may be immediately used in thermodynamic simulation. Also, the state
di
agrams of open systems may be used to find correspondence between values of
and
.This makes new
theory and following from it Method of Chemical Dynamics (MCD, [6]) immediately available for practice.
Practical advantage of the method of chemical dynamic
s is not restricted by opportunity to avoid usage of
coefficients of thermodynamic activity. The method, for instance, also leads to new in principle opportunity to
simulate internal equilibrium of a system with subsystems at different thermodynamic temper
atures (like in
plasma).
To conclude we would like to mention that open chemical system is by definition coupled with another open
system, more exactly, with its compliment to a bigger system. Changing the control parameters may cause an
adjustment of the
whole system to new equilibrium state through the bifurcations area, and one will observe it
as a system of coupled oscillators [5]. If they are convergent the system eventually may achieve internal
equilibrium.
Addressing to a skeptical reader, we’d like
to underline that
o
ur non

traditional term of the basic equation
already existed in chemical thermodynamics in form of excessive thermodynamic function, having different
meaning and origin. This work gives alternative description in relation to an external
impact and offers unified
concept of open chemical systems where true and open equilibrium, bifurcations and chaos are logically tied
1

11
together in unknown before combination. We just tried to find out what has been lost or hidden when
chemical system, the
major object of chemical thermodynamics, has been idealized as an isolated entity.
REFERENCES.
[1] Prigogine, I.
From Being to Becoming
; W.H. Freeman: San Francisco, 1980.
[2] Zilbergleyt, B.
Russian J. Phys. Chem
., 1985,
59(7
)
, 1059.
[3] de Donder, T.; van Risselberge, T.
Thermodynamic Theory of Affinity;
Oxford University Press; Stanford, 1936.
[4] Gyarmati, I.
Non

Equilibrium Thermodynamics;
Springer

Verlag; Berlin, 1970.
[5] Epstein, I., Pojman, J.
An Introduction to Non

linear Chemical Dynamics
; Oxford University Press: New York, 1998.
[6]
Zilbergleyt, B.
Thermodynamic equilibrium in open chemical systems
; //
LANL Printed Archives
,
Chem
.
Ph
ysics
,
19.04/2000,
http://arXiv.org/abs/physics/0004035
.
[7] Zel’dovich, Ya.
J. Phys. Chem.(USSR), 1938,
3
, 385.
[8] Klimontovitch, Yu.
J. Tech. Physics Letters (USSR)
, 1983,
8
, 1412.
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