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This chapter deals with the determination of Hansen solubility parameters
(HSP) for the solid surface of cellulose acetate phthalate (CAP) by inverse gas
chromatography in the temperature range 333.15 - 393.15K. The number average
molar mass of the polymer was K - 2534.12 and density at 25 C? was 0.266 glcm).
Cellulose acetate phthalate is produced by reaction of phthalic anhydride with a
partial acetate ester of cellulose, in presence of sulphuric acid. CAP contains 21.4-
26.0% of acetyl groups, and 30.0-36.0% of phthalyl groups. The structure of CAP is
shown below in Fig.6.1.
Fig.6.1 The structure of cellulose acetate phthalate (CAP)
Cellulose esters have been extensively used as binders, additives, and coating
applications.' Cellulose acetate phthalate (CAP) belongs to cellulose ester family,
which presents large field of biotechnoiagical applications due to its
biocompatibility.' For instance, it has been used as entwic coating of drugs, which
should survive in the acidic environment of the stomach, but should be released and
absorbed in the intestine.' Cellulose acetate phthalate is commonly applied to solid-
dosage forms either by coating from organic or aqueous solvent systems or by direct
compression. Concentrations generally used are 0.5-9.P! of the core weight. The
addition of plasticizers improves the water resistance of this coating material, and
formulations using such plasticizers are more effective than when cellulose acetate
phthalate is used alone. Applications of HSP data of cellulose acetate phthalate and
polyethylene glycols were discussed in tablet film coating3 The biodegradability of
Polymethylmethacrylate - cellulose acetate phthalate blend has been studied by four
different methods namely, soil burial test, enzymatic degradation, degradation in
phosphate buffer and activated sludge degradation followed by water absorption
tests to support the degradation studies.' The blends of PMMA with CAP have
pharmaceutical appl i~at ions.~ Therapeutically, cellulose acetate phthalate has
recently been reported to exhibit experimental microbicidal activity against sexually
transmitted disease pathogens, such as the HIV-1 retrovirus?'
Inverse gas chromatography (IGC) is one of the most versatile, fast and
reliable technique to determine the Hansen solubility parameters of non volatile
substances? The determination of Hansen solubility parameten for the solid surface
using IGC data has been proposed by Voelkel 'O based on the adsorption model
described by Snyder and ~ a r ~ e r . " In the IGC method the polymer which is to be
characterized is placed in the column and the volatile solute probes are injected so
that the probe is at infinite dilution in the stationary phase. Hildebrand solubility
parameter and Hansen three component solubility parameters are usehl in
predicting the solubility behavior of a polymer in various solvents and plasticizers.
'"I4 Hansen solubility parameter data have been found lo be applicable to examine
different intermolecular interactions at the solid surface^.'^ The solubility parameter
data is also useful to correlate polymer compatibility with other polymers and in
designing coating formulations. HSP data are particularly useful in solid phase
extraction for the selection selection of a suitable ~olvent . '~ ~umerous papers have
been published on the characterization, based on the HSP data, of non volatile
materials such as inorganic salts, fibers, clays, pharmaceutical powders, cellulose,
pigments, hydrocarbons, polymers and polymer blends."~*@
6.1. Specific retention volumes V:
In IGC the retention is mainly governed by the surface and bulk interactions
of the solute with the stationary phase. This interaction can be characterized with the
measured specific retention volume,^:, which can be related to thermodynamic
quantities. The specific retention volumes for the interaction of a solute on a solid
surface can be calculated using the relation
where, t, is the retention time of the probe solute and t,is the retention time of
methane measured at the column temperature. F is the flow rate of the carrier gas
measured at room temperatureT,, w is the mags of the stationary phase. P, is the
water vapour Pressure at T, . The flow rate of the carrier was measured at the
column outlet at T,using a soap film flow meter. The carrier was saturated with
water vapour existing in the soap film flow meter before flow rate measurement.
Therefore P, is subtracted from P, in Eq.6.1. J is the James and Martin correction
factor which depends on the inlet, P,, and outlet, 6 , pressures calculated wing the
following relation.
The specific retention volumes, v:, for 21 solute probes are calculated
according to Eq.6.1 in the tempmature range 333.15 - 393.15 K . The V , values are
listed in Table 6.1. The V; values are decreasing with increase of temperature for all
the solutes. The retention diagrams drawn between In Y: versus 1/T are shown in
Figs. 6.2 -6.9 for all the solutes. The retention diagrams for all the solutes are linear
which indicate that in the temperature range studied there was no phase change in
CAP. In the measured temperature range CAP is in the solid phase. Therefore the
retention of the solute probes is mainly due to adsorption of the solute on the solid
surface of CAP.
Table 6.1. The specific retention wlums, v,Y , (m31g) of solutes on cellulo~
acetate phthalate in the ternpmture range 333.15 - 393.1 5K.
Solutes
n-octane
Acetone
Ether
Methanol
Ethanol
Benzene
Toluene
2-Propanol
2-Butanol
Dichloromethane
Trichloromethane
Methyl acetate
Ethyl acetate
1-Butyl acetate
1 ,4-dioxane
THF
Fig.6.2 Retention diagrams of n-pentane (*), n-hexane (o), n-heptane ( A ) nnd n-
octane (*) on CAP in the temperature range 333.15-393.15K.
and J -butan01 (7) on CAP in the temperature range 333.15-393.15K.
Fig.6.4 Retention diagrams of esters: methyl acetate (I), ethyl acetate (e) and I-butyl
acetate (A) on CAP in the temperature range 333.1 5-393.15K.
Fig.6.5 Retention diagrams of dichloromethane (r), trichloromethane (o) on CAP in
the temperature range 333.15-393.15K.
Rg.6.6 Retention diagrams of 2-alcohols: 2-propanal (0 ) nnd 2-butanol (9) on CAP
in the temperature range 333.15-393.15K.
Fig.6.7 Retention diagrams of acetone (r) and diethyl ether (*) on CAP in the
temperature range 333.15-393.1 5K.
Fig.6.8 Retention diagrams of benzene (I), toluene (a) on CAP in the temperature
range 333.15-393.15K.
Fig.6.9 Retention diagrams of I, 4-dioxane (o), tetrahydrofuran ((I) on CAP
in the temperature range 333.1 5-393.15K.
6.2. Weight fraction activity wffdent, a,"
The partial molar weight fraction activity coefficient, R; for the interaction
of a solute at infmite dilution on CAP surface cm b nl.4 to V: by the following
equation2'
where MI is the molar mass of the solute and R (8.314 J ~ ' m o l . ' ) is gas constant.
9 4 and are molar volume, saturated vapour pressure and second virial
coefficients of the solute at temperature T. Vl and 4 were estimated in the
temperature range 333.15 - 393.15K following the standard methopds reported in
the litmature and the necessary parameters required in the evaluation were taken
from the literature. 2' The second virial coefficients, B,, were calculated by
utilizing the Tsonopoulos m e t h ~ d . ~ V, , f: and R,, values are given in Tables. 2.5,
2.6 and 2.7 in chapter 11.
The weight fraction activity coefficients at infinite dilution, Inn" , for 21
solute probes were calculated according to Eq.6.3 in the temperature range 333.15 - 393.15 K. The Innm are listed in Table.6.2. The Inn" values are decreasing with
increase of temperature. The Inn" values are increasing with increase of chain
length in the n-alkane series. The magnitude of In 0" is a measure of interaction of
the solute probe with the solid surface of CAP. The various types of molecular
interactions viz. dispersive, polar-induced polar, dipolar and hydrogen bonding
contribute to the values of 1nR". In the n-alkane series only dispersive interactions
are present between CAP and n-alkane. The dispersive interactions are increases
with increase of hydrocarbon chain length and hence InR" values increased with
increase of n-alkane chain length. In the case of 1-alcohols and 2- alcohols both
hydrogen bonding and dispersive interactions are present in between CAP and
alcohols. As the chain length increases, the strength of hydrogen bonding decreases
and dispersive interactions increases. Therefore the variation of Innm with chain
length in alcohols depends on the resultant of the two interacting effects. The results
indicate that the dispersive interactions dominate over hydrogen bonding in alcohols.
Esters can form hydrogen bonds with -OH groups present on CAP surfaces. The
variation of ha" with chain length in esters depend on hydrogen bonding, dipolar
and dispersive interactions. The results indicate that the dispersive interactions
dominate and hence InQm values are increasing with increase of chain l a & in
esters. The variation of 1nRm with carbon number in n-alkanes, alcholos and esters
is shown in Figs. 6.10 to 6.13. The increase in Inn" with chain length is almost
linear in n-alkanes and esters at all t e m p e r a m . However in 1-alcohols the
variation of In Q" with chain length is linear at lower temperatures rmd nonlinear at
higher temperatures.
Table 6.2. The partial molar weight fraction activity coefficients, InRm, of solutes on
cellulose acetate phthalate in the temperature range 333.1 5-393.1 5K.
Temperature (K) Solutes
333.15 343.15 353.15 363.15 373.15 383.15 393.15
n-Pentane 2.736 2.627 2.463 2.360 2.300 2.252 2.288
n-Hexane 3.264 3.094 2.894
n-Haptane 3.637 3.493 3,306
n-octane ' 3.974 3.892 3.640
Acetone 2.956 2.791 2.668
Ether 2.792 2.716 2.624
Methanol 2.144 2.085 1.989
Ethanol 2.219 2.141 2.073
I -Propanot 2.340 2.256 2.173
1-Butanol 2.412 2.434 2.261
Benzene 2.823 2.733 2.671
Toluene 3.166 3.015 2.912
2-Propanol 2.625 2.561 2.430
2-Butanol 2.768 2.672 2.515
Dichloromethane 1.585 1.499 1.406
Trichloromethane 1.822 1.687 1.605
Methyl acetate 2.089 1.923 1.772
Ethylacetate 2.522 2.305 2.128
1-Butylacetate 3.012 2.926 2.904
1,4-dioxane 2.424' 2.242 2.048
THF 2.405 2.347 2.200
Fig.6.10 The variation of In Qm with hydrocarbon chain length, of n-alkanes at seven
temperatures on CAP.
Fig.6.11 The variation of Inn" with carbon nuniber, Z, of I-alcohols at seven
temperatures on CAP.
Fig.6.12 The variation of Innm with carbon nurnbcr, Z, of 2-alcohols at seven
temperatures on CAP.
Fig.6.13 The variation of In R" with carbon number, Z, of n-acetates at seven
temperatures on CAP.
6.3. Flory-Huggins interaction parameter,
The Flory-Huggins interaction parameter, x;, for the solute on the solid
surface of CAP is related to In R" as fol~ows.~'
M,u* ~ ; = l n R , ~ +In- - 1 v, (6.4)
where u2 is the specific volume of the polymer. For CAP polymer specific volume is
given by 3.759 cm31g. The Flory-Huggins interaction parameter, xP,, was evaluated
using Eq. 6.4. The XI", values are given in Table.6.3. The z; is a measure of the
interaction of solute, I, with the polymer CAP, 2, at infinite dilution of solute on the
CAP. For n-alkanes X; values are positive and grater than 0.5. The variation of
X; with temperature is shown in Figs.6.14 to 6.19 for eight youps of solute probes.
The X; values are decreasing linearly with increase of temperature. As shown in
Fig.6.20 at any one temperature x;", values are increasing with increase of chain
length in the n-alkane series. The trend for aromatic compounds was similar to n-
alkanes, where xP; values are increasing with increase of size of the compound. As
shown in Fig.6.21, the xP; is not linear with the chain length of I-alcohols. This
behaviour may be interpreted primarily using the values of and p, as well as
how these values are changing with size of the solute. The X; is inversely
proportional to V; and p, of the solute. In n-alkanes x,", increased with increase of
chain length; here p, is crucial, which is higher for lower n-alkanes. In 1- alcohols,
due to hydrogen bonding, the vapour pressure is relatively less and the X; values
only slightly decreased with increase of chain length. The V i values are importnnt in
determining the trend in 1- alcohols. On the other hand, in esters, x;", values are
slightly increased with increase of chain length, which is due to slightly higher
vapour pressures in esters compared to I - alcohols. The variation of x,*, for aters
was intermediate between n-alkanes and 1- alcohols.'
Table 6.3. Floty-Huggns interaction parameter, X; , of solutes at infinite
dilution, on cellulose acetate phthalate in' the temperature range 333.15 - 393.15K.
Temperature (K) Solutes
333.15 343.15 353.15 363.15 373.15 383.15 393.15
n-Pentane
n-Hexane '
n-Haptane
n-octane
Acetone
Ether
Methanol
Ethanol
I -Propano1
1 -Butan01
Benzene
Toluene
2-Propanol
2-Butanol
Dichloromethane
Trichloromethane
Methyl acetate
Ethyl acetate
I-Butyl acetate
1,4-dioxane
THF
Fig.6.14 The variation of xT2 values with temperature on CAP for n-alkanes : n-
pentane ($1, n-hexane (I), n -heplane (*) and n- octane (A) .
Fig.6.15 The variation of xr2 values with temperature on CAP for I-alcohol:
methanol (I), ethanol (a), 1 -propano1 (*) and I - butanol(o).
T(K)
Fig.6.16 The variation of ~ 7 ; values with temperature an CAP for esters: methyl
acetate (m) ethyl acetate ( 0 ) and n- butylacetate (0).
Fig.6.17 The variation of xrz values of benzene (8) and toluene (o) on CAP in the
temperature range 333.15-393.1 5K.
Fig.6.18 The variation of xT2 values of acetone (m) and diethyl ether (a) on CAP in
the temperature range 333.1 5-393.15K.
Fig.6.19 The variation of 1r2 values of 1, Cdioxane (m) and tetrahydrofuran (a) on
CAP in the temperature range 333.15-393.15K
Fig.6.20 The variation of X; with carbon number, Z, of n-alkanes at seven
temperatures on CAP.
z
Fig.6.21 The variation of xh with carbon numba, Z, of 1-alcohols at seven
temperatures on CAP.
6.4. Hansen solubility parameters
According to Hildebrand 26 the solubility parameter for a volatile
solute is related to its cohesive energy, E , and molar volume, y as
follows.
However the application of the above equation to polymers and nonvolatile
substances is not possible due to their negligible vapour pressure. Further, the
Hildebrand solubility parameter model proposed for regular solutions may not be
able to describe adequately the solubility behavior when polar and hydrogen
bonding solvents are involved in the system. Hansen addressed this problem by
introducing the three dimensional solubility parameter model.'* According to
Hansen theory the total cohesive energy is approximated as a sum of three
independent contributions arising from dispersive, E d , polar, E,, nnd hydrogen
bonding , E,, interactions respectively.
E d = Ed + EP + Eh
Therefore the total solubility parameter is derived as follows. By dividing Eq. 6.6
with molar volume V, we get
6; =6,? +6: +6,2 (6.8)
wheres,, 8, and 6, are the Hansen solubility parameters (HSP) representing
dispersive, polar and hydrogen bonding components rapectively. The determination
of HSP by IGC for materials which are in the liquid state at the temperature of the
experiment have been reported extensively in the literature. However, studies
relating to the determination of HSP for solid rr~atcrialv by IGC are scanty. Voelkel
'O developed a method for the determination of HSP for a solid surface by IGC
following the Snyder-Karger adsorptioq model." Accordingly, the energy of
adsorption of test solute '1' on solid adsorbent '2' is given by the energy balance
expression
-AE* = E~~ = ( ~ ~ ~ j ~ ~ ( ~ ~ ~ j ' ~ = Y , (d l ) (6.9)
where BEA is the of adsorption, v, is the molar volume of the test solute,
and ED are the cohesive mergis for the t a t solute '1' and the a d s o h t '2',
and Elz is the energy of cohesion for the interaction between 'I ' and '2'. S, and
are solubility parameters of solute ' 1 ' and the adsorbent '2'. Introducing Eq.6.6
in Eq.6.9 gives.
- A ~ A = ( E I Z ) d + ( E 1 2 ) p t (E12)D (6.10)
or
- a E A = V, (#&+ G f 8 + G:&) (61 1)
The energy of adsorption A,@ is related to the specific retention volume by the
following equation.
- A E A = ~ T l n t const (6.12)
From Eqs. 6.1 1 and 6.12 one can derive the following relation.
R ~ l n v ; = v,G;'&t VISPG$ + v16:6: +const (6.13)
where d, 6{ and i$ are the dispersive component, polar component and hydrogen
bonding component of Hansen solubility parameters for cellulose acetate phthalate.
Linear multiple regression on Eq.6.13 has been performed using the software
Orginpro 7.0. The specific retention volumes of 21 solutes at one temperature have
been used in the regression analysis at one time. The Hansen solubility
61 and 6: of the solid surface of CAP are obtained from the
coefficients of the multiple regression analysis. The statistical analysis has been
repeated at other temperatures and the results are yjvm in Table.6.4. The solute
&tag:, 6/' and 8; required in this evaluation are given in Table 2.9 in Chapter 11.
The Hansen solubility parameters for the 21 solutes at 298.15K were taken
from the literature.'' The d , s/' and values at the experimental temperatures
were calculated using the ,relations proposed by Hansen and Beerbower. 24 " The
HSP of all the solutes at 363.15K and their temperature gradients are given in Table
2.9 in chapter 11. The solubility parameter data can be related to many different
physicochemical characteristics and used for the interpretation of several
phenomena, such as miscibility, solubility and adsorp t i~n .~ The HSP of a CAP can
be determined using Eq.6.13. The three components of the Hansen solubility
p-&ers,,jf, &f and 8 , of the 21 solutes were fitted as a fbnction of the left
hand side of fhe E9.6.13 by multiple regression d y s i r at esch tan-. Tbc mfficients of the multiple regression war used to obfain the dispaive
componm,&, Polar component, dl, and hydrogen bonding component. 6: of the
solid surface of CAP. The three components ,$. ~f and ,$ wen used 'in Eq.6.8 to
calculate the total solubility parameter, 6:. The solubility parameter values along
with the e ~ ~ o r s in these components are given in Table.6.4. The variation of the HSP
with temperature is linear in the temperature range studied. The values of the
Hansen solubility parameters are in the following order:
5;1> &>sf The & values are higher compared to ;Sp which may be due to the presence
of relatively higher hydrogen bonding interactions than dipolar interactions between
the polar solutes and the CAP surface. The emrs in the&, fif and hj are
decreasing with increase of temperature. The values of correlation coefficients, r,
given in Table 6.4 indicate that the regression model was better at lower
temperatures than at higher temperatures. The relative errors in HSP are calculated
using the relation.
S Relative error = = .
X
where s is standard deviation and ;is mean value. For example the relative errors
in&, and & at 333.15 K are, 0.37,0.51 and 0.19 respectively. A comparison of
relative errors in the three components indicates that they are in the following order.
s:<bi </-Sf
Further, the variation of the solubility parameters with temperature is shown
in Fig.6.22. & and 6 values are decreasing with increase of temperature where as
Jf values are nearly constant. The plots are used to extrapolate the data to 298.1 5K
and the extrapolated results are also included in Table.h.4. During the application of
CAP in the design of membrane materials? in the coating formulations and as
adsorbent materials, the Hansen solubility paran~et!xs are often required at room
temperature or at 298.15 K. Therefore the extrapolated HSP given in Table.6.4 can
be utilized to understand the behaviour of CAP in presence of different materials at
ambient temperatures.
Table 6.4. The Hansen solubility parameters for solid surface of CAP calculated
using Eq.6.13, at seven temperatures: dispersive, &, polar, &g , hydrogen bonding,
& and 6: total solubility parameter. r, is the correlation coefficient, of the
regression.
T(K) 8 WPa) In 85 (MPa) In 6: (MPa) 'I2 ,$ (MPa) '" r
*Extrapolated data
Fig.6.22 The variation of Hansen solubility permeters with temperature:
dispersive, 8 (a),, polar, 6{ (o), hydrogen bonding & (m), total solubility
parameters 6; (x) the plots are drawn using the data given in Tables 6.4 and
extrapolated to 298.15K.
6.5. Enthalpy of adsorption
The enthalpy of adsorption,LW,, for the adsorption of a solute on solid
surface of CAP has been calculated using the following relation. '
The values of enthalpy of adsorption, AHa, are given in Tnble.6.5. AH,,
values are negative for the 21 solutes. The AH, values are more negative for polar
solutes compared to n-alkanes. This may be attributed to the fact that in n- alkanes
only dispersive interactions present where as in polar solutes in addition to
dispersive interactions the CAP surface also exhibit the dipolar and hydrogen
bonding interactions. The variation of Mi, with hydrocarbon chain length in n-
alkanes and 1-alcohols has been shown in Fig. 6.23. The AH, vnlues are linearly
increasing with increase of chain length in n-alkanes where as in I-alcohols the
variation is not linear.
Table 6.5 Enthalpy of adsorption, -AH,, (k.Jmol-') of solutes on the cellulose
acetate phthalate (CAP) surface in the temperature range 343.1 5 - 403.1 5 K.
Solutes - AH, (ldmof')
Acetone 16.1 1k0.32
Diethyl ether 19.4kk0.53
Methanol
Ethanol
I -Propano1
1 -Butan01
Benzene
Toluene
2-Propanol
2-Butnaol
Dichloromethane
Trichloromethane
Methyl acetate
Ethyl acetate
1-Butyl acetate
1 ,4 -~ ioxhe
THF
Fig. 6.23 The variation of enthalpy of adsorption, -AH, with carbon number, Z, of
n-alkanes (m), and alcohols (I) on CAP solid surface.
Conclusion
The surface thermodynamic properties for cellulose acetate phthalate are
determined by IGC. The surface thermodynamic p r o w = for cellulose acetate
phthalate are determined by IGC technique. The partial molar weight fraction
activity coefficients, Innm, and Flory-Huggins interaction parameter, x i , are
calculated using the measured specific retention volumes, V: .The Inn" and X:
values have been used to understand the interactive ability of CAP surface with
different solutes and as function of temperature. The specific retention volumes of
21 solute probes have been used to calculate the three components of Hansen
solubility parameters. The dispersive component, b j , and hydrogen bonding
component, s:, are decreasing with increase of tempernturc where as polar
component, 84, is nearly constant in the temperature range studied.
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