235
Fluid Phase Equilibria, 12 (1983) 235-251 Elsevier Science Publishers B.V., Amsterdam
PERTURBED
HARD
EXAMINATION K.
and
AIFl
of of
A
EQUATIONS
SIMPLE
OF
EOUATION
Process
Chemical
Sciences,
(Received
in The Netherlands
STATE
OF
OF
THE
REAL
SECOND
LIQUIDS.
I.
ORDER
NEZBEDA
I.
Institute Academy
SPHERE
OF
-Printed
January
165
Prague
1982;
8,
Fundamentals,
02
6,
accepted
Czechoslovak
Czechoslovakia
in
final
form
May
16,
1983)
ABSTRACT K.
and
state
of
Aim,
the
Utility
I.
Fluid
a
perturbed
of
the
hard
An
both
attempt
their
is
temperature
properties. perturbed
hard
sphere
made
to
some
sphere
and
a
sphere
equations
simple
equation
12: of
square is
in
general
state
well
based
parameters
terms
of
for
of
state
are
a
orthoof
of
the
independent on
on
fluid
examined
conclusions
of of
235-251.
supercritical,isotherms
interpret
equations
a
equation
for
contributions sub-
dependence
Finally,
hard of
Equilibria,
theory
three-body and
Perturbed Examination
Phase
Barker-Henderson
densities
fluids.
1983.
I.,
liquids.
order.
of
inclusive
and
real
second
simplified
baric
Nezbeda,
the
simple
equation molecular
family
of
drawn.
INTRODUCTION Theoretical
statistical
state
aim
fluid
rather
data.
Nonetheless,
to a
usually than
interpret, few
if
molecular
require
very
which
be is
understanding
at
obtaining
an not
accurate However,
advantage predict,
considered quite
equation
origin
this
the
beyond
the
the
approach
other
hand, of
is
of of
experimental
that
by
it
means
chemical its
equation
equations properties
with
properties
regardless
else
of
agreement
bulk
empirical
anything
useless
of the
On
any
calculations‘on the
accurate
parameters.
justification. hardly
mechanical
at
allows of
theoretical
of
state
than
an
interpolation
range
of
available
(EOS) scheme
experimental
data. In liquids
the
last
has
0378-3812/83/$03.00
made
two
decades
considerable
the
statistical progress
mechanics
and,
0 1983 Elsevier Science Publishers
B.V.
thanks
only
engineers
of to
simple
various
can
236
ingenious now
integral
available
simple
liquids
1980;
Smith
are
not
two
reasons:
about
within and
complexity
of
the
actual
intermolecular
of from
on
suitably
number defined
interactions an
directly
the
construct
sphere
of
density-dependent attractive
diameter) (F or
the
first
derived
version
permanent
make
use
attempts
well.
The
primary
can,
at
least
in
principle,
is
the
stems
repulsive gave systems
resulting term to
become
it.
EOS
with
e.g.
Based
in
is
either
popular
or
combined
EOS
being
on
to the
same
temperature-
terms
accounting
Leland,
1980
and
of
the
the
being
above
type
Contemporary known made
question
accurate to
is,
lead
to
is
hard
improve
whether
an
the
van
improvements sphere
the
the term
correction
such
accurate
der
of
an
and
approach
relatively
EOS.
This
paper
perturbed
hard
practical
calculations.
employing
assess and
of
1873.
are
as
by
has
see
fluids of
finding
semiempirical
review
EOS
in
term simple
the
temperature-
is a
to
1979).
Historically, equation
a
(with
for
allowed
intermolecular
related
it
is
reference
leading
somehow
result,
spheres
forces.
Robinson,
original
EOS or
for
originally
of
This
of
the
purposes
hard
for
and
with
are
role
with
Consequently,
series
of
scheme.
predominant
part
why
compensate
the
structure.
repulsive 1977).
practical
EOS
and
and
the
is
theory
theories
theories
mechanical
for
: the
Waals
by
hard
the
liquid
perturbation
expansion
statistical
Chao
the
of
(Boublik,
by
of
To
such
uncertainties
the
degenerate
mechanical
knowledge
as
(ii)
parameters
correlation
statistical
the
model.
may
another
of
al.,
because
That
potential
which
establishing
a
potential
et
theories
and
version
approach,
into
the
the
are
classical
(Boublik
interactions.
pair
of
calculations
theories
simplified
variables,
procedure
primarily
a
such
state
Success
way
a
with
of
rigorous
given
However,
(i)
methods
properties errors
practical
on
to
1978).
theories,
the
to
inaccuracies
this
Henderson,
combined
forces
perturbation
calculate
pseudoexperimental
calculations
depend
to
directly
the
usually
and
us
applicable
practical
rise
equations
allowing
the
limits.
sphere
a
The
of EOS
-Henderson
theory
parameters
adjustable,
part,
equations The
quite
family
first
for
general these employed
goal
a
of
state
and
their
the
paper
is
of
series
perturbed
is
examine
of
hard
equations
a square-well we
uf
by
based
on
a
of
devoted
to
application
in
two-fold.
sphere
finding
fluid. first
papers
its
EOS we
try
potentialities
simplified
Barker-
Leaving
all
all
utility
the
First,
the
EOS (i.e.
to
237 ability
to
correlate
orthobaric
densities we
Second, potential of
make
and
properties
conclusions to
the
of
the
entire
of
state.
equations
and
find
a link
independent
by
the
data)
sub-
only
paper
family
of
possess
of
between
the
equation
of
isotherms.
We
more
general
simple
This
is
molecular
it possible EOS.
for
obtained
quantities.
existence
an
the
super-critical
makes
means
of
physical
the
parameters
liquids
of
to
because
of
of
kinds
both
attempt
importance
interpretation
apply
and
an
parameters
high
the
particular
to
believe
predict
the
that
most
validity
and
perturbed
of
hard
sphere
pair
potential
THEORY Equation by
of
approximate,
an
effective oo
USW
because
Red
= -E
for
d(R
0
for
R -z R,
d
well,
and
is a hard
potential
with
correctly From that
the
their
on to
pressure.
the
Axilrod-Teller
was
estimated
and
Dividing perturbation of
the
total
parts,
Helmholtz
a pair
argon
of
real
for
et
+ upert,
to
this reproduce
1971)
it follows
negligible up to
50
and per
effects,
contribution
the
al.,
potential
potential
is able
three-body
whose from
the that
al., not
represent the
of
known
molecules.
et are
P, may
(Barker
energy,
It is
forces
account
u = uref
is a depth
(Barker
potential
pair
free
true
parameters
analytically
coworkers
the
chosen of
To
E
potential.
pressure,
pressure Barker
the
three-body
consider by
diameter,
liquid
non-additive
total
of
properties
study
contribution
the
sphere
appropriately
basic the
the
potential,
(1)
is a range
R.
of, simplicity,
square-well
for
where
of
state
We
perturbation
cent we
to theory
1968).
into the
F, assumes
reference
and
perturbation a form
(Boublik
expansion et
al.,
1980): F/(NkT)
= F ref/(NkT)
For
first-order
F(l)
the
= 2rp
7 0
+ F(')/(kT) perturbation
gref(r)
upert(r)
+ F(*)/(kT)* term r* dr
we )
+
...
(2)
have: (3)
238 where
p
is
function
the
number-density For
(rdf).
compressibility is,
the
only
the
the
than
therefore
distribution
local
used;
(Barker
has
radial
usually
better
approximation
approximation
is
term
is
marginally
compressibility
g
second-order
approximation
however,
latter
and
this
the
and been
approximation
macroscopic
Henderson,
chosen
1976).
because
The
of
simplicity: m F(2)
= -*PkT
where
subscript
For
the
system d c
(2) aP
pair
is R <
ghs(r)
hs
i
hs
denotes
potential
the of
straightforward, R,
and
tupert(r)12 hard
form =
otherwise.
the
the
s
(4)
system. choice
uhs(R;d)
For
dr
sphere
(1)
uref
zero
r2
of
and
u
pert
first-order
the
reference -E
= term
for
then
it
holds: F(‘)/(kT) where the
p
x
3
= Pd
integrals
method that
the
RO
, T” in
due
square
to
and
sphere
and Renon
rdf
and
x
(5)
analytically,
=
equals
Ro/d.
s
(19 76)
(5)
unity
order
In
we
based
on
beyond
the
the
to
express
follow
the
approximation range
of
the
-
11/(4”P)
we1 1 potential, dr
r2
Approximation general,
(6) it
The
E 7’ d
is
hard
r2
shown for
+
ap hs (,p)T,”
[kT
.
be
justified
R,
>s
is
accurately
(Carnahan
+ y2
-
and
for
R,/d
=
1.5
but,
-
in
d. described
Starling,
by
the
1969),
y3 ,
(1
(7)
Y)3
= 11p’/6.
Using
usual
thermodynamic
factor,
i!
=
z
+
*z(l)
= Zhs
3 R,/3
to
= y
=
any
reference EOS
1 + y
dr
(6)
was
sphere
(P/PkT)hs
ghs(r)
correct
Carnahan-Starling
where
(4)
,
1 r 2dr
ghs(r
= T/(E/k),
Eqns
Ponce
hard
ghs(r)
;
:,
= -2nPx(l/Tx)
where
A.z(~~)
After
evaluating
finally
get
P/pkT,
may +
dz(2)
stands the
+
for the
following
relationships
be
expressed . . .
the
the
LQ(3b)
to
(2), (8)
due
to
compressibility
expressions
Eqn
,
contribution
isothermal
compressibility
similarly
for
three-body from
AZ
(i):
Eqn
forces. (7)
we
239
T"
a~(')
= -4yX3
(4y
+
- 2y3).(1
+ 1oy*
- y)3 ,
DL AZ(~)
Tx2
= -6yCI
- 6y21
"c
a1 -
- 6y2C
ay
(9)
,
(10)
ay
where D = 1 + 4y
+ 4y2
(1 - Y)~/D
c =
I = 13/3
+
of
the
only
These
the
free
energy
was
quite
well = y2
YN where written
where
y
with
sphere
though
to
introduce
the
- 0.08477~
+ 0.05499y2
The
constant.
the
~~(1
and
factor
al.
found of
to
that
the
this
form
(12)
’
corresponding
compressibility
make et
contribution
Pade' approximant
0.07516
(7)
first
may
order
be conveniently
form, + 5y
of
to
given
EOS
of may
density any
+ 15y2
(11) state
seem
in
- 3y3)
,
Eqn
(13)
define
the
perturbed present
we
have
polynomials,
of
first
order
as
PHS2
retained the
order
EOS,
hard
paper.
preferring
Throughout
the
second
is denoted
the
in the
complicated,
appearing
equation
whereas
(lo),
(13)
simplifications.
sphere
PHSl
and
investigated rather
the
additional
hard as
by
Numerical
through
equation
perturbed
referred
in
not paper
l/TX
involving
is
the
equation.
procedures EOS
sphere
and
the
the
pair
fourth
by
we
to Barker
the
reference
- 0.31570y2
the
orders
hard
numerically sphere
forces
due
= ,/(,d').
(PHS)
The
hard
three-body result
+ 0.88445~
to
all
term
the
0.74240
Expressions Even
the
represented
= 20y2
x
of
analytical
calculated
in a simplified
4~(~~)
the
contribution
y is a force
contribution
.
available
authors
F(3b)dg
, (11)
(C - 1)/(24y)
the
(1968).
t y4
,
Concerning use
T"
- 4y3
derived
is essentially
diameter
reduced
range
potential
parameter,
(d), of
model the
the
depth
attractions and
were
temperature
a four-parameter of
the
equat ion.
potential
(A)
are
subject
to
independent
we1
directly adjustment. three-body
The
1 (E/k),
re lated The force
to
240 strength
has
(y),
al., To
study
were
the
the
best
for
argon
fit
of
(Aim,
It
violated
and
weighted
least
estimates. opinion
the
the
resulting
(Barker
et
(Pe
P is
the
been
t
all
taken
the
It
of
the
The
where
a
and
V
of
T;)2
2 ST i
in
this
data
point
(V”c
-
V8
are
the
in in
K,
expression
=
(14)
(14)
proved
have
a
and been
the
isothermal
be
reduced
one-step a
set
of
calculated
coexisting P-V
on
to
has
to
temperature
these
Pe, calculations
which
function
true
paper
0.0015 the
deleted,
of
and respective
this
sp
vo 1 umes
and
the
. During
values
(14)
molar
experimental
v;
for
3
sVG and
= 0.01
given
V;)2 2
so
model as
phases.
data
outside
the
was
(TP -
if1
ihood
is to
respectively,
: fugacities
used
1 i kel
experimentally
+
errors
therefore
For
are
function
orthobaric
reported sT
objective
function
region
index
VE,
equality
objective
N =
Pt,
the
two-phase
the
procedure,
parameters, satisfy
been
assumptions 1981)
maximum
the
V:)2
between
computations
has
optimization
minimization
-
phases,
= 0.00015 = 0.00015 VF, and sv sVl. G orthobaric data the first term in insignificant.
an
experimental
as
the
errors.
VI
distinguish
the
objective
criterion
2
vapor
invariably
parameters
represent
sVL
estimated
In
variables.
(V;
pressure, and
and
are
of (Aim,
the
all
from
+
saturation
e SK
than
obtain
was
Pt)2
2 sP
liquid
superscripts values;
-
some
objective
to
to
algorithm
parameters
that
these
as
iterative
optimization
minimized
so The
an
of
fact
subject
parameters,
symmetric
method
rather
parameters
+
EOS level
case
symmetric
the
are
Tt)2
2 ST
our
appropriate
function -
(Te
in
using
values
for
the
likelihood
likelihood
the
EOS
of
consideration.
by
estimates
the
equilibrium
have
that
maximum
variables
objective
where
clear
allows
evaluate
=
1980)
the
most
it
under
HanEil,
square
the as
determined
s2
literature
temperature
maximum
Nevertheless,
problem,
To
so
each
property
is
with
at
minimizing
and
1981).
our
the by
(Rod
associated
to
from
dependence
separately
estimated
function
of
taken
temperature
evaluated
were
s,
been
1971).
runs
(Pf +
over
-
P;)2
2 sP all
points
(V;
-
V:’
+
(15) considered
on
an
isotherm.
241 When
orthobaric
simultaneously function s3
had
= m.S,
where the
and
to the
the
isotherm
EOS
data
parameters,
were
the
used
objective
form
t S2
,
(1’3)
m is a factor orthobaric
liquid-phase
determine
from
data
the
point
range
1 to 0.67N
relatively
to the
used
to over-weight
points
on
liquid
isotherm. The
optimum
determined
parameters
at
by minimizing
the
the
critical
objective
point
have
been
function
(17)
f where
subscript
the
model
Ptc,
and
t V, were d2P
(Z)2
To
DISCUSSION additional
with our
krypton,
EOS
liquid
factor,
the
(iv)
coefficient. individual The
compilation were
also
basis
of
stemming
typical
methane.
for
critical
Given TE,
criterion
The
uncertainties
complex
liquids,
properties fit
- volume point
from
we
of
the
the
PVT
data,
and
(v)
to assess
the
relative
in
tried Eqn
source
the
(Vargaftik, from
of
triple
of
data,
(iii)
the
second
virial
relevance
of
(8).
range the
(i) data
compressibility
supercritical also
on were
orthobaric
(PVT)
critical
we
argon,
focused
both
- temperature
and
molecules
namely
We
taken
point.
coordinates
the
more
simple
simultaneous
pressure
from
The
the
models
critical
investigated
MPa.
the
(18)
to
(ii)
terms
temperatures 100
and
phase of
at
critical.point
problems
only
data,
location
on
interaction
xenon,
orthobaric
the
.
AND
applied
and
localized
avoid
connected
quantities
values,
-0
+(z)2
RESULTS
c denotes
parameter
variables to 450
PVT
1975). the
state point
NBS
krypton
from
the
work
of
methane
from
API
Res.
Project
data
employed
In addition, monograph
Theeuwes 44
covers,
K and
and
was the
(Gosman Bearman
(1968).
roughly,
pressures
up
to
Vargaftik's PVT
et
data
al.,
(1970),
for
1969), and
for
argon for
1
R,/d
vapor
89.83 90.11 100.22 118.81 132.11 140.72 152.43 177.89
1.825 1.828 1.771 1.679 1.624 1.592 1.552 1.479
1.781 1.795 1.787 1.774 1.719 1.682 1.682 1.562 1.542 1.492
R,/d
to PHS2
are
equation.
and
are
by PHSl
volumes
K
76.02 74.44 75.84 77.81 86.17 92.64 92.93 117.76 122.56 135.93
E/k,
data
uncertainties
correspond
experimental
and
3.7054 3.6515 3.5997 3.5459 3.5376 3.5398 3.5441 3.5502
110.00 130.00 150.00 170.00 175.00 180.00 183.00 186.00
liquid
3.3758 3.3549 3.3306 3.3140 3.2949 3.2666 3.2309 3.1968 3.1781 3.1531
87.28 94.39 102.85 108.58 114.99 124.19 134.83 142.69 145.99 149.00
'Both
d, 1
fit of orthobaric
T, K
Best
TABLE
0.08789 0.36710 1.0330 2.3380 2.7880 3.2880 3.6180 3.9800
therefore
not
shown.
%
The
parameters
d, E/k,
%
0.02 0.02 0.26 0.45 1.41 1.11 1.11 1.17
-0.07 -0.03 to.03 0.11 0.12 0.70 2.05 4.05 6.34 10.02
AP,
and
within
PHSE
well
0.08791 0.36717 1.0357 2.3485 2.8272 3.3246 3.6581 4.0268
0.10126 0.20258 0.40541 0.60859 0.91304 1.5275 2.5850 3.6899 4.3099 5.0168
P, MPa
equations
2.25 4.40 8.33 9.11 11.1
0.92
1.08 1.74 2.67 3.36 4.56 6.03 a.78 13.2 16.4
AP.
PHS2
PHSl
and
0.08870 0.37537 1.0785 2.5328 3.0421 3.6528
by PHSl
e
0.10242 0.20617 0.41612 0.62838 0.95348 1.6116 2.7556 4.0160 4.7183
P. MPa
equations'
t h a_n
0.10133 0.20265 0.40530 0.60795 0.91193 1.5199 2.5331 3.5464 4.0530 4.5596
argon
exDt1
reproduced
me
PHS2
P, MPa
and
243 Subcritical
region
Comparing performs EOS
the
much
of
the
term
improvement
et
of
this
as
strength
as
the
For
but
both
(y
of
argon
=
some
lead
the
PHS2
the
inclusion
three-body
data
trial
isotherms
erg.cm', of
the no
and
liquid
values to
into brings
data
and
73.2~10~~~
rather
equation
forces
orthobaric
orthobaric
value
well
for
equations,
respects, for
of
theoretical
1971)
PHS2
all
region.
treatment
the
al.,
force
and in
accounting
in
simultaneous use
PHSl
better
the
the
see
Barker
three
body
slight
deterioration
on
subcritical
of
results. Therefore
we
restrict
the
of
Eqn
to
forms
results
obtained
for
those
for
argon
argon
and
methane.
For
orthobaric
volumes is
are
superiority Table
very
of 1.
good
a
low
become
the
calculated
equation orthobaric
methane
displayed
on in
the
by
the as
selected
Table
mostly
PHSl
data
pronounced
results
largely
facts
of
the
EOS
significant is
PHS2
documented
equation
is
pressure
critical
region
for
with
about
equilibrium
equation the
isotherms
1 along
to
The
positive
the
the
analogous on
in
region
Since
inadequacy
pressure.
over
but
term.
deviations
whereas
of
more
The
are
discussion
small
high
the
AZ (3b)
the
xenon
typically
temperatures,
approached. are
our
PHS2
fit
of
and
base
or
too
the
The
at
departures
can
data
by
discussion
exclusive
krypton
negligible
reflected
in
we
the
(8)
the
is
argon
and
effective
potential
parameters. It
is
interesting
equation values
of
these
are
second
The
as
if
the
not
m
is
the
individual
related shown
terms
factors.
in
to
the
Table
2.
with
opposite
important
despite
the
PHS2
hard-sphere Since
signs its
in
Characteristic
the
the
first
inclusion
relatively
two of
the
small
=
was
of
unity
data
factor thus
to
PVT
by
the
from
reality; N in
and
m
in
be
and
PHS2
Eqn
confirming
0.67
included
found
liquid-phase
incapable
of
orthobaric equation
describing
data
simultaneously.
yields,
roughly,
the
follows:
distorted,
equation -
and
equation the
treatment
for
is
how
value.
results -
note
compressibility
are
large
term
PHSl
reasonably Such
factor
very
order
absolute
to
contributions
compressibility terms
to
contribute
the
VB
optimization,
(16)
the
term
in the
the
existing
the
fit
of
orthobaric
departure
expression
representation
of
for of
S,
data the
(14)
orthobaric
is
244 TABLE
2
Relative contributions the compressibility
of factor
individual
Z/Zhs
= Zhs/zhs
terms +
in
the
Z(')/Zhs
PHS2
equation
+ Z(2)/Zhs
near triple point
liquid vapor
0.0005 0.962
1 1
-1.0390 -0.027
0.0395 -0.011
near T_
liquid vapor
0.067 0.405
1 1
-0.972 -0.527
0.039 0.068
data
ranges
IAP] ~10
from
per
= 0.85;
T/Tc good
at
the
the
P (
PC,
pressure The
and
good
cent,
where
parameters data
increasing
temperature.
is of
the
about
of
yx
by
The
high
the
isotherms the
pressure
per
at
cent is
higher
cent
at of
more
at
very
pressures
50
MPa.
liquid-phase
evaluated
becoming
a
zc,
The
minimum
parameter
value et
is
viz.
from
pronounced
zc
(1971).
increases
equations
of
critical
that
by
namely
with
value
of
zc
at
x
the
the
the
yielded
and
the
proceed shifts
PHSP
family,
by
1.35.
three-body
marginal
we
PHSP
relative
=
improvement
approximately
As
again
this
given
0.3280
only
corresponding
al.
as
parameter,
surprisingly,
indicate
the
third x.
values
to
to to
yx
greater
X.
equation,
fails
to
that
higher as
well
as
describe
region.
region
expected,
equation
fourth
Barker
zc
Supercritical
of
deviations per
isotherms
those
AZ (3b) term)
the
brings,
minimum
other
adequately
of
the
= 0.02,
given the
fit
~20
treatment from
factor,
the
well,
(without term
values,
As
differ difference
of
potential
Introduction
all
function
equation
y
10
maximum
lAVg/ but
cent, to
simultaneous
compressibility
a
interaction at
per up
the
to
and
subcritical
increase on
up
cent,
of
somewhat
only,
critical
equation
for
per
point
The
PHS2
temperatures
IbPl 5 0.5
based data
orthobaric
width
low
representation
deviations
orthobaric
Critical
at
lbVLl ~0.7
to
the
without of
argon,
experimental critical
examination
AZ (3b)
the
krypton, data
point.
deviations
At
the
to
xenon,
is
exhibit
of
term least
T/T, the
ability
correlate and
of
methane
satisfactory
Q, 1.02, trend
typically, as
the
PHSE
supercritical
follows:
revealed in
close the
that
the
vicinity maximum
IAPI 2 0.5
per
245 cent 100
at
1 MPa,
MPa.
values
Temperatures equation Potential
% 1.3
the the
0.8,
and
are
both
well
\APl fit
above
4 per
PVT
range
cent
at
data
mentioned
cent,
maximum
respectively.
reproduced
supercritical
10 per
5 of
by the
PHSE
investigated.
parameters
Potential particles
parameters Dealing
usually The
better
variables extent,
a real
as
the
model
the
less
can
be expected.
to assess
potential
and
the
parameters
thus
many-body
and
an
less the
by looking
obtained
from
discussion
we
the
approximate
at
parameters
fitting
for model
calculations to
state
possible,
the
of
state
potential
parameters
It is therefore
EOS
pair
on
to compensate
inadequate
the of
isolated
depend
system,
in order
for
sensitivity
of an
cannot
adjustable
calculations
used,
properties
speaking,
with
treated
approximate
reflect
strictly
and,
variables.
used.
whole
10 MPa,
0.5,
volumes
the
at
isotherms
At T/T,
become
and
over
cent
higher
considerably.
deviation
are
5 per
5 for
However,
improves
are
(API
to a certain
behavior
of
the
the
EOS
to experimental
the
subcritical
data. the
In since The
following
similar
problem
conclusions is,
that
the
parameters
is not
one
extrapolate
cannot Effective
diameter, properties pair
as
interactions. are
in their
size
There
are
several
explicit
dependence
decrease
with
kinetic
energy,
obvious. who
The
d on
whereas
simplest purely
theory
of
core
of
the and
so
at
to be
the
a small
theories
increase
due
providing
In
general,
d should
of
increase
in
density
power-type
of
is known
in pressure.
because
of d is that
molecular part
densities
so that
on
several
other
EOS
liquid
variables.
dependence
sphere
for of
type
mechanical
state
repulsive
as well.
region
repulsive
increment
temperature its
any
hard
interest in terms
other
enormous
statistical of
hard
to each
an
increasing
investigated
any
of
critical
effective
diameter
d parameter:
close
produces
The
primary
collision
to the
quite
of
region,
region
region.
interpreted
Further,
hi'ghly sensitive molecules
quantity the
in the
diameter.
be easily
such
this
on
supercritical dependence
function
over
sphere
is the
It can
focus
in the
temperature
a simple
hard
d,
reasons.
hold
to
is much
less
Rowlinson
potentials
and
(1964), found
that d *
(l/T)l'n
,
(‘9)
246 where
n
defines
(1967a) was
the
define
d
parametrized
(1972).
for
Chandler,
sphere
diameter
and is
The
equation
These
seem
be
smooth
obtained
for
data
The
0.92
and
indicating
that
their
Henderson
integral,
by
Verlet
liquids
is
theory
integral
but
of
to d on
at
obtained on
functions
of
methane
nob1 e gases.
In
an
diameters
(Sticking
dependence
*
sphere
experimental
parametrization.
simple
and an
which and
that
the
d
Weis
of
hard
depends
now
on
density.
to
consider
by
by
potential of
(1971).
again
Barker
theory
theory
Andersen
hard
to
repulsions.
Lennard-Jones best
given
and
effective
PHSP
of perturbation
the the
temperature
T/ Tc
their
Presumably
Weeks,
both
steepness
in
a
PVT
simple
T/T,
>
0.90
then
slightly for
we
from
minimum
employed
do
not
that
for
at
temperature
model
simple
dependence
differs
with
the
1.
to
picture
shallow
increase methane
Table
temperature
somewhat
d exhibit
even
d
the
in
amenable
physical The
fitting
shown
temperature
density).
calculated
by
are
again, may
thus
be
oversimplified. Influenced models
we
d
+
=
do
For
all
by
substances
The
b parameter
for
methane
same.
diameters of
does
the not Even
the
varies
depth
properties
are
proved
different though
of
all
a
was
in
by
to
potential
1964)
in
range
at from
same
in
a
molecule
the
to
form
very by
our
calculations
yielding approaching
for as
krypton that
per
to
in
to
d,
may
hardly than
be the
cent.
10.4
observed
correspond
-
c/k
o/k
almost Tc:
depth a
15
E/k
the as
potentials It
to
this
the
the
size
interpreted. hard-core
we same tends
the
obtained
at
that from each
more
fit.
this
has
sampled temperature
wide
range,
However,
frequently
gases
macroscopic
and
relatively
overall
well,
effective noble
parameter starting
a
potential
for
indicates
well:
covering
the
of
quantity
K.
as of
of
8.5
range
and
2
can
The
sensitive
guesses
estimates
about
do
pair
10
very
being
larger
unique
accurate
not
Tc
model.
as
about
was
temperatures
Concerning
while
well. be
(20)
lower
1981).
somewhat
Kihara
Eqn
at
(Nezbeda,
parameters,
always
by
good
error
the
potential
initial final
temperature
hard-core
correlation very
the
nearly
other
seem
diameter.
level
simple (Rowlinson,
experiments
two
do
used
Depth
been
found
is
core
that
the was
T % T,,
was
the
hard
We found
E/k,
other
result
It
scattering of
the
at
which
high-energy meaning
and
examined
the
reasonable
of
Kihara
Rowlinson’s
d, (l/T)l’b
qualitatively still
the
applied
to
with attain
241
higher
values
shown
in
The same
depth
but
of
for
an
e/k
=
the of
for
independent
of
that
for
more
Tc
+
E/k
values
0.4
with
T,
the
[(T
of
e/k
- Tt)/(Tc
steepness
of
fluids
useful
is
Tc
to
may
Tt)lK
are
versus
the
to
the et
relate
al.,
c/k
to
accounting
possess
a
form
I
(21)
T.
subcritical
examined
related
parametrization
-
E/k
for
be
(Hirschfelder
approaching
calculated
four
more Simple
T
may
potential
purposes
E/k
values
the
potential
realistic
constants.
in
K defines
sets
square-well
a
material
0.5
Representative
range.
practical
increase
where
the
1.
parameter
1964),
to
within
Table
Based
on
regions
parameter
the
entire
we
have
be
set
K can
found equal
3. Range
of
attraction of
more
attraction. range
of
realistic
1964),
but
Values always
potential
otherwise of
with
level,
parameters.
There
Ro/d
= A1
gives
a
the and
sum
so
have
A2/(E/k)
+
A3(E/k)
parameters
side
that
or
R,/d
of
et
obvious.
equation even
R,/d
are at
the
the
two
and
E/k
interpretation,
the
al.,
same
(like
but
temperature relation (22)
only
correlation
holds
considered.
is
not
the
parameters
between
stronger
that
relating
other
depth,
physical
found
which
provides
is PHS2
correlation
temperature-independent
two
substances
right-hand
a
weaker
we
R,
the
combinations
offering
exhibit
of
to
Hirschfelder
potential a
rules
R,, e.g.
fitting
so
However,
strictly
between range
+
from
algebraic
11)
combinations
dependence.
(see
interpretation
indicating
-
semi-empirical
potential,
increasing
are
e/k[(Ro/d)2
are
models
obtained
decreasing
these
an
R,/d
temperature
e.g.
There
square-well
In a
minor
approximately
over
Eqn
the
(22)
the
contribution
proportional
equation
entire last to
directly
temperature term the
on
the
total
to
(c/k)-l.
Second
virial
Though rather
it
coefficient is
known
insensitive
provide
a
EOS.
Eqn
B(T)
=
useful (8)
(2/3)
the
source
gives w
that
to
d
3
B(T) {l
-
the
second
actual
form
of
information
in
a
virial
coefficient,
of
pair
the
about
the
potential, parameters
B(T),
is
it of
may the
form
[(Ro/d)3
-
1]
(1
+
0.5
T")/T")
(23)
248 We
have
Eqn
found
(23)
provides d
is
to
reasonable from
to
A
question properties and
(22).
The
results
for
used
We
have
temperatures,
d,
E/k,
values same
the
ability
and
of
manner of
R,/d
B(T).
If
as
that
Eqn
(23)
unchanged. to
parameters
predict
calculated evaluated
ranged
definite
low
the
potential
be
parameters
have No
argon.
in
(20)),
whether
versa.
very
experimental
(Eqn
may
the
of
practically
is,
vice
using
for
parameters
temperature
remains
liquid by
with
properties
B(T)
properties
fair
vary
typical
equation
exception
independent
correlation
liquid
correlate
from
an
temperature
allowed
found
with
that,
with
from
density
B(T)
from
from
excellent
conclusion
Eqns
for
can
evaluated
low
the
(20)
methane
therefore
PHS2
through to
be
only
drawn.
CONCLUSIONS We
have
investigated
simplified We
fluid.
have
equation
by
and
sub-
both
been and
the
case.
~z(~~) term
(Eqns with
to
be
to
bulk
paid
The a
some
to
be and
way
to
of
for
a
the
critical
and
on
square-well point,
an
main
conclusions
l/T*
has
not
least
the
second-order
in At
agreement good
is EOS
to
(13))
should
may
the
itself,
or
Anyhow,
the
been
be
been
of
PHS2
vicinity
of
any
simple
improved
by
this of
the
was
that
of
attention
non-additive
not
term
incompatibility
feel
contribution
The
the
However,
the
to term
but
inadequacy
we
able
required.
feature have
effects.
either
used.
is
everywhere
a common
three-body
estimating
results hard
are
extremely
sphere
parameters
have
quite
due
approach
of
we
order
the
the
function
priori
The
data.
which of
smooth
a
the
based
the
this
ought forces
properties.
effective is
may (12)
the
be
point,
account
This
EOS of
properties
isotherms
quantitative
to
performance
into
first PVT
if out
critical
taking
the
introduced
The
general
parameters.
two-phase
turned
the
EOS.
sphere
theory
densities,
super-critical
of
the
be
for
orthobaric
the
hard
perturbation
follows.
equation
equation of
of as
represent must
perturbed
searching
examining
interpretation summarized The
the
Barker-Henderson
the from
the
considered improve
the
sensitive
diameter, and of
structure the
it
d.
seems
the
that
function
and might
the
the d
d of
to
consider
of
the
dependence
itself
= d(T)
dependence be
value
temperature
properties
temperature
results
to
The
may
of
or
at
least
be
determined
molecules
alone.
only,
possible
one
density
As
dependence
d
249
This
as well.
would
partly
remove
perturbation
terms
but
the
d on
could
be
simply
to
the
density
Comparing significant actual R,/d
value. and
e/k,
two-parameter somewhat
For
to
the
found
the
EOS
equations The
properties to
the
that
point
calculations (simply
the
PHS2 and
consider along
the
reported LIST ; & N ; RO
the
OF
Ro/d
to
play to
the
to but
to the
is able
two-phase
still
find
and Eqns
(20)
equation
(as
given
by
the
ability
has
simple
of
been
the
data
of
above, the
two
the
PVT
theoretical
outlined course.
We
directions
at
with
two
the
basis
temperature,
T'
= T/(E/k)
to of
describe
the
fact
clearly
investigations
results
in variable
function temperature
and
Daubert
encourages
the
SYMBOLS
error
and
assumptions the
PHSE
Hence,
hard sohere diameter Helmhoitz free energy radial distribution function Eoltzmann constant number of molecules pressure center-to-center distance attraction range of potential experimental
the
equations
same.
continue and
temperatures
(22))
Graboski
on
accurately
Detailed
through
the
derived
promising.
above
reduced
1.5.
PVT
describe
methane
is practically
in due
TX
of
reasonably
important.
by
approach
objective absolute
al.
value
of
semiquantitatively
we
argon
that
to
region
on
surface
rather
estimated
two-
reported
performance
a
exhibits et
liquid
those
a
its
parameters
strictly
and
parametrized
equation
sX S T
such
be essentially equation
set
to
the
equation
the
and
critical
revealed
defined
PHSZ of
the
PVT
of
same.
Redlich-Kwong-Soave (1978))
dependence
Dzialoszynski
orthobaric
region
temperatures
subcritical
with
seem
PHS2
(1976).
inferior
supercritical
that
comparative equation
the
insensitive
out
a similar
Renon of
not
the
fact,
than
and
results
inclusive
lower
close
the
between
turns
this
correlation
the
from
how
rather
coupling
PR equation
obtained
is
fact
Ponce
the
simultaneous in the
Despite
does
are
investigated
flexibility
examined
whereas
at
Due
of
remains
parameter
results
EOS
they
E/k
complexity
parametrized.
the
EOS.
methane
question
and
greater
-parameter (1980)
d,
role
the
X
will
be
us
to
260
packing fraction, compressibility Greek Y x Y Ax i P x P
letters three-body
y = nd3P/6 factor
interaction
force
constant
reduced force constant, yx = y/(cd') or deviation in contribution, change, depth of the potential well reduced range of attraction, X = R,/d number density, p = N/V 3 reduced density, px = pd
quantity
X
Subscripts C critical point hs hard spheres t triple point Superscripts experimental value e t true value three-body interactions (3b) Abbreviations EOS equation of state PHSl perturbed hard sphere (equation), PHS2 perturbed hard sphere (equation), PR Ponce-Renon (equation) PVT - volume - temperature pressure rdf radial distribution function
first second
order order
REFERENCES Aim,
K., 1981. Estimation of vapor-liquid equilibrium parameters. Paper presented at the 7th International CHISA'81 Congress, Prague. API Res. Project 44, loose-leaf data sheets, extant, 1968. Selected Values of Properties of Hydrocarbons and Related Compounds. Thermodyn. Res. Center, Texas A&M univ., College Station, TX. Barker, J.A. and Henderson, D., 1967. Perturbation theory and equation of state for fluids. The square-well potential. J.Chem.Phys., 47: 2856-2861. Barker, J.A. and Henderson, D., 1967a. Perturbation theory and equation of state for fluids. II. A successful theory of liquids. J.Chem.Phys., 47: 4714-4721. Barker, ~J.A. and Henderson, D., 1976. What is liquid? Understanding the states of matter. Rev.Mod.Phys., 48: 587-671. Barker, J-A., Henderson, D. and Smith, W.R., 1968. Three body forces in dense systems. Phys.Rev.Lett., 21: 134-136. Barker, J-A., Fisher, R.A. and Watts, R-O., 1971. Liquid argon: Monte Carlo and molecular dynamics calculations. Mol.Phys., 21: 657-673. Boublfk, T., 1977. Progress in statistical thermodynamics applied to fluid ohase. Fluid Phase Eauilib.. 1: 37-87. Boublik, T.,'Nezbeda, I. and Hlavaty, K:, 1980.-Statistical Thermod namics of Simple Liquids and Their Mixtures. Elsevier, Azztz&z Carnahan, N.F. and Starling, K.E., 1969. Equation of state for nonattracting rigid spheres. J.Chem.Phys., 51: 635-636.
251 K.-C. and Robinson, R.L., Jr., (Editors), 1979. E uation of Chao, and Research. Advan.Chem.Ser. & State in Engineerin Ch Sot., Washingtzn. On the equation of state of Del Rf!; F. and Arzola, C., 1977. argon. J.Phys.Chem., 81: 862-865. Dzialoszynski, L., Fabries, J.-F., Renon, H. and Thiebault, D., 1980. Comparison of analytical representations of thermodynamic properties of methane, ethane, and ammonia. Ind.Eng.Chem. Fundam., 19: 329-337. Gosman, A.L., McCarty, R.D. and Hust, J.G., 1969. Thermodynamic Pro erties of Argon from the Triple Point to 30 &i) Atmospheres. Nat.Stand.Ref.Data Ser., N~tKB~:.~~~~~ur,es 0.
Graboski, 'M.S. and Daubert, T.E., 1978. A modified Soave equation of state for phase equilibrium calculations. 1. Hydrocarbon Proc.Des.Develop., 17: 443-448. systems. Ind.Eng.Chem., Hirschfelder, J.O., Curtiss, C.F. and Bird, R.B., 1964. Molecular Theory of Gases and Liquids. John Wiley & Sons, New York. Kreglewski, A W'lhoit R C and Zwolinski B.J 1973. Application'of'hard ;phere equation of state ti real fluids. J.Chem.Eng.Data, 18: 432-435. Lan, S.S. and Mansoori, G.A., 1976. Perturbation equation of state of pure fluids. Int.J.Engng.Sci., 14: 307-317. Leland, T., 1980. Equations of state for phase equilibrium computations. Paper presented at the 2nd International Conference on Phase Equilibria and Fluid Properties, West Berlin. Nezbeda, I., 1981. Simple pair-potential model for real fluids. Part III. Parameter determination and a revised model for spherical molecules. Czech.J.Phys.B, 31: 563-571. Ponce, Analytical equation for the L. and Renon, H., 1976. Helmholtz free energy of a pure fluid, using the perturbation theory and a square well potential. J.Chem.Phys., 64: 638-640. Rod, V. and HanEil, V., 1980. Iterative estimation of model parameters when measurements of all variables are subject to error. Comp.Chem.Engng., 4: 33-38. Rogers, B.L. and Prausnitz, J.M., 1971. Calculation of high-pressure vapor-liquid equilibria with a perturbed hard-sphere equation of state. Trans.Faraday Sot., 67: 3474-3483. Rowlinson, J.S., 1964. The statistical mechanics of systems with steep intermolecular potential. Mol.Phys., 8: 107. Smith, W.R. and Henderson, D., 1976. Some corrected integral equatiqns and their results for the square-well fluid. J.Chem. Phys., 69: 319-325. Theeuwes, F. and Bearman, R.J., 1970. The p,V,T behavior of dense fluids. II. The p,V,T behavior of liquid and of dense gaseous krypton. J.Chem.Thermodyn., 2: 171-177. Vargaftik, N.B., 1975. Tables on the Thermophysical Properties of Liquids and Gases. e ition , 0 n (2 n Verlet L and Weis, J.-J.. 1972. Equilibrium theory of simple liqiids. Phys.Rev.A, 5: 939-952. Weeks, J.D., Chandler, D. and Andersen, H.C., 1971. The role of repulsive forces in determining the equilibrium structure of simple liquids. J.Chem.Phys., 54: 5237-5247.