Kaushalendra Chaturvedi1, Harsh S Shah1, Kajal Nahar1, Rutesh Dave2, Kenneth R Morris3. 1. Arnold and Marie Schwartz College of Pharmacy and Health Sciences, Long Island University, Brooklyn, New York 11201, United States. 2. Division of Pharmaceutical Sciences, Arnold and Marie Schwartz College of Pharmacy and Health Sciences, Long Island University, Brooklyn, New York 11201, United States. 3. Lachman Institute for Pharmaceutical Analysis, Arnold and Marie Schwartz College of Pharmacy and Health Sciences, Long Island University, Brooklyn, New York 11201, United States.
Abstract
In the literature, it is reported that eutectics lead to the enhanced dissolution of a poorly soluble compound. However, the solubility theory suggests that since crystal structures of two components are unchanged that all else being equal, the dissolution rates of a fused mixture (FM) should be the same as a physical mixture (PM). The influence of crystal lattice energy on dissolution profiles was investigated using the PM and FM. Experimental phase diagrams constructed using differential scanning calorimetry data were compared with those theoretically derived. Deviation of the experimental phase diagram curves from the theoretical model indicates the nonideal behavior of both systems (ibuprofen/poly(ethylene glycol)-6000 and acetaminophen/caffeine). Both the binary systems showed an increase in the dissolution rate of the PM and FM. However, the dissolution from the PM was comparable with the FM's dissolution profile. The theoretical solubility calculations using the modified solubility equation showed that the use of the eutectic temperature instead of the drug's melting point should give a 3-4-fold increase in drug solubility. However, the correlation between dissolution and solubility calculation showed that the FM did not improve the dissolution when compared with the respective PM's dissolution profile. The proposed explanation is that the unchanged crystal lattice energy in eutectics still limits the solubility and therefore the dissolution rate.
In the literature, it is reported that eutectics lead to the enhanced dissolution of a poorly soluble compound. However, the solubility theory suggests that since crystal structures of two components are unchanged that all else being equal, the dissolution rates of a fused mixture (FM) should be the same as a physical mixture (PM). The influence of crystal lattice energy on dissolution profiles was investigated using the PM and FM. Experimental phase diagrams constructed using differential scanning calorimetry data were compared with those theoretically derived. Deviation of the experimental phase diagram curves from the theoretical model indicates the nonideal behavior of both systems (ibuprofen/poly(ethylene glycol)-6000 and acetaminophen/caffeine). Both the binary systems showed an increase in the dissolution rate of the PM and FM. However, the dissolution from the PM was comparable with the FM's dissolution profile. The theoretical solubility calculations using the modified solubility equation showed that the use of the eutectic temperature instead of the drug's melting point should give a 3-4-fold increase in drug solubility. However, the correlation between dissolution and solubility calculation showed that the FM did not improve the dissolution when compared with the respective PM's dissolution profile. The proposed explanation is that the unchanged crystal lattice energy in eutectics still limits the solubility and therefore the dissolution rate.
The
solubility and permeability behavior of drugs play a major
role in bioavailability. Bioavailability of poorly soluble drugs from
the Biopharmaceutics Classification System (BCS) class II category
has been a major challenge for the pharmaceutical industry as before
a drug can be absorbed from the gut, it must first be soluble in the
relevant body fluid.[1] Examples of drugs
with solubility problems include ibuprofen (IBU), chloramphenicol,
fenofibrate, digoxin, griseofulvin, phenytoin, and sulphathiazole
in their free base or free acid form.[2] The
solubility of new drugs has been decreasing for years as new more
complicated molecules have been identified through the high-throughput
target-specific screening. Several approaches have been employed to
enhance the solubility of poorly soluble compounds including (1) nanosizing
and micronization, (2) formation of amorphous or metastable crystalline
phases alone or in a polymer matrix, (3) formation of eutectic mixtures,
(4) co-crystal and salt formation, (5) complexation, and (6) solid
dispersion of the drug in the hydrophilic polymer matrix.[3−13]Solid dispersion is widely used in the development of dosage
forms
for enhanced solubility and dissolution of an active pharmaceutical
ingredient (API).[11] Solid dispersions can
be classified into two broad groups based on the solid state of the
drug substance in the system, i.e., amorphous and crystalline. The
amorphous form of hydrophobic drugs is typically known to improve
dissolution in aqueous media over the crystalline form.[14,15] The disadvantage of developing the amorphous system is its long-term
stability and phase-transformation issues.[16−18] Therefore,
the solid dispersion delivery system where the drug is maintained
in a crystalline form is usually viewed as the best alternative. Crystalline
solid dispersions, in which the drug and carrier exist in a crystalline
form, can be categorized into eutectics and monotectic. Eutectic mixtures
are often confused with and categorized as solid dispersions, but,
in fact, the eutectic mixture is a mixture of two or more components
that do not chemically interact but at a certain ratio inhibits the
crystallization process of one another, resulting in a system with
a lower melting point compared to either of the pure components.[19] An eutectic system is the combination of APIs
and/or excipients, depending upon the desired performance. A simple
eutectic mixture consists of two compounds, which at the eutectic
composition are completely miscible in the liquid state but show little
or no miscibility in the solid state.[20] The crystal structures in a eutectic mixture remain unchanged, save
disorder introduced during formation, from the parent components,
indicating i.e., the eutectic is not a co-crystal or different crystal
form of either component. Ideal eutectic compositions and eutectic
temperatures can be estimated with the modified van’t Hoff
equation.[21,22] The literature suggests that eutectic mixtures
may or may not be a simple physical mixture (PM) of two different
crystalline phases. Based on the fusion properties of the pure components,
they may have defined microstructure formation compared to the physical
mixture.[23−25] In the literature, it has been reported that the
formation of eutectics enhances the drug dissolution rate due to the
formation of microstructures, solid solutions, interfacial disorders,
or melting point depression. However, a less studied dimension is
the effect of crystal lattice energy on the dissolution rate of eutectics,
consisting of a drug and crystalline polymer. One reason for the lack
of the study is the limited understanding of the mechanism by which
a drug’s dissolution rate is supposedly increased from a eutectic
mixture. It has been reported that the factors that affect the eutectic
formation include a thermodynamic function of the melting point and
heat of fusion, both the parameters are a measure of enthalpy and
entropy.It is hypothesized that, if the microstructure, i.e.,
the particle
size of the target analyte(s), remains constant in the physical mixture
(PM) and fused mixture (FM), any enhancement in eutectic dissolution
depends primarily on the formation of that microstructure, i.e., effective
particle size/surface area and crystal quality (i.e., degree of disorder)
in a eutectic mixture. If it was true, the physical mixture and fused
mixture is expected to show similar dissolution profiles. Significant
improvement in the dissolution rate is more likely due to the solubilization
effect from highly soluble “carrier” compounds in the
eutectic couple. Therefore, the question is, can a fused mixture contribute
to the enhanced solubilization of poorly soluble compounds and if
so, what is the underlying mechanism for enhancing the dissolution?In this work, the authors have attempted to assess eutectic formation
predictability and understand the contribution of crystal lattice
energy to the dissolution behavior of APIs in two different binary
mixtures. These are ibuprofen–poly(ethylene glycol)-6000 (IBU/PEG)
and acetaminophen–caffeine (APAP/CAFF). Ibuprofen and caffeine
are known to form a eutectic with PEG-6000 and acetaminophen, respectively.
PEG-6000 is a large hydrophilic molecule compared to ibuprofen, which
is expected to improve ibuprofens’ wettability, leading to
an increase in solubility (at least a local cosolvent effect). The
literature supports that the IBU/PEG system increases the dissolution
rate and extent of ibuprofen.[26−28] However, that enhancement may
be due to a combination of the particle size, crystal quality, and
the solubilization effect of PEG-6000.[24,29−31] To understand the involvement of crystal lattice energy in dissolution
enhancement of eutectics, it is necessary to control (or eliminate)
the solubilization effect of the polymer or hydrophilic matrix, PEG
in the current study. To that end, the APAP/CAFF system was selected
as a model system. The APAP/CAFF system consists of two small molecules
with approximately similar aqueous solubility under the conditions
used, so there should be no significant improvement in solubilization
imparted between them. The specific aims of this study were (a) understanding
the contribution of crystal lattice energy in dissolution, (b) developing
analytical methods to determine the eutectic formation, and (c) studying
the dissolution behavior of the eutectic system.
Results
and Discussion
Phase Diagram and Differential
Scanning Calorimetry
(DSC)
The binary temperature vs composition (T–χ) phase diagram provides graphical information on
the equilibrium phases present at a given temperature. The phase diagram
explains the behavior of two immiscible crystalline solids from a
completely miscible melt.[7,32] A binary T–χ phase diagram can be generated using the Schröder–van
Laar (SVL) equation (eq ), which is based on the ideal mixing theory.[33] Similarly, thermal transition data from DSC can be used
to generate an empirical phase diagram. In this research, phase diagrams
were generated using DSC data and the SVL model. Predicted and experimental
phase diagrams were generated to understand the role of ideal mixing
in the formation of eutectics. The closer the agreement between the
experimental curves from the phase diagram and the SVL-predicted model,
the more ideal the system is said to be.where R is the gas constant,
ΔHfusion is the enthalpy of fusion
of the pure component, TM is the melting
temperature of the pure component, TE is
the measured eutectic temperature of the system, and X is the mole fraction of the components.
Ibuprofen–Poly(ethylene
glycol)-6000
System
The Schröder–van Laar (SVL) equation
model was used to predict the ideal eutectic composition of the IBU/PEG
system. The experimental values for DSC analysis are shown in Table . The DSC curves were
overlaid to construct an IBU/PEG experimental phase diagram. Both
the predicted and experimental phase diagrams show that the addition
of PEG leads to a decrease in the melting point of ibuprofen as it
approaches the eutectic temperature (TE). At the eutectic composition, the binary system is invariant. When
the eutectic mixture is heated above the eutectic temperature, the
mixture melts into a liquid. This defines the solidus boundary for
the IBU/PEG binary system. DSC scans of IBU/PEG solid dispersions
below and above their respective eutectic compositions exhibited two
endothermic events, with the lower-temperature endotherm corresponding
to the melting of the eutectic mixture and the high-temperature endotherm
due to the melting of either the pure excess polymer or the excess
crystalline drug (Figure a). Theoretical curves from the phase diagram were compared
with the experimental results, showing the difference in eutectic
composition as well as the eutectic melting temperature. According
to the theoretical curves, the eutectic composition is 5% in ibuprofen
with a eutectic temperature of 59 °C. However, the experimental
phase diagram shows that ibuprofen is 35% of the total eutectic composition
with a 48.91 °C TE (Figure b). The differences reflect
the nonideal behavior of the IBU/PEG system.[33]
Table 1
Experimental Results from DSC Analysis
of the IBU/PEG Binary System
melting
or depressed melting temperature of (°C)
T
ratio of IBU/PEG
ibuprofen
PEG-6000
temperature at solidus curve
(°C)
100:0
76.32
90:10
74.93
46.9
75:25
72.27
48.76
50:50
58.69
46.88
35:65
50.95
50.95
48.91
25:75
55.62
46.98
10:90
59.96
47.82
0:100
60.32
Figure 1
(a)
Overlaid DSC thermograms of the IBU/PEG system. (b) Comparison
between the phase diagram generated using the Schröder–van
Laar (SVL) equation model and DSC study.
(a)
Overlaid DSC thermograms of the IBU/PEG system. (b) Comparison
between the phase diagram generated using the Schröder–van
Laar (SVL) equation model and DSC study.
Acetaminophen–Caffeine
System
Similar to the IBU/PEG system, the SVL model was used
to construct
a phase diagram for the APAP/CAFF binary system. DSC thermograms of
different ratios of APAP/CAFF were overlaid to construct an experimental
phase diagram. Experimental values from DSC analysis are mentioned
in Table . The theoretical
eutectic curves were then superimposed on to the experimental phase
diagram to understand the ideal behavior of the eutectic mixture.
DSC thermograms of neat acetaminophen showed an exothermic event at
56 °C, indicating the recrystallization of amorphous APAP (Figure a).[34] The DSC thermogram of neat APAP shows the presence of Tg at 21.6 °C, which confirms the recrystallization
of amorphous APAP (Figure b). However, the neat APAP does not show the exothermic event
at 56 °C in contrast to the binary mixtures. This might be because
the neat APAP was tested under DSC as received while binary mixtures
were premelted. APAP/CAFF at different ratios, except at the eutectic
composition APAP/CAFF system, showed two endothermic transitions.
The first endothermic event represents the eutectic temperature (TE), while the second endothermic event represents
the melting of the pure component (TM).
The second endotherm indicates the presence of the component, which
is present in excess in the binary mixture. The SVL model predicted
the eutectic composition at 75% APAP with a eutectic temperature of
approximately 149.41 °C. However, the experimental results showed
a significant difference in both eutectic parameters. Based on the
experimental results, APAP/CAFF forms a eutectic system when 60% of
APAP is present in the system and TE is
close to 131.46 °C. The deviation of experimental eutectic parameter
values from the theoretical curves indicates the nonideal behavior
of the eutectic mixture (Figure c). Compared to the IBU/PEG system, APAP/CAFF is closer
to the theoretical curves, which indicate less involvement of entropy
of mixing during the formation of the APAP/CAFF eutectic system. The
higher entropy of mixing could explain the complete offset of the
IBU/PEG curve from the theoretical curve and predicted eutectic parameters.
Experiments were carried out twice at each composition level, and
the results indicated that the shift in the solidus curve temperature
is about ±2 °C (data showed in the Supporting Information). The shift in the solidus curve temperature is
because of small but unavoidable experimental or analytical variations.
Table 2
Experimental Results from DSC Analysis
of the APAP/CAFF Binary System
melting
or depressed melting temperature of (°C)
ratio of APAP/CAFF
APAP
CAFF
temperature at solidus curve (°C)
100:0
169.30
90:10
161.48
133.35
80:20
155.1
134.31
60:40
131.46
20:80
210.62
134.99
10:90
224.34
133.63
0:100
237.38
Figure 2
(a) Overlaid
DSC thermograms of the APAP/CAFF system, (b) DSC thermogram
of neat APAP as received from the vendor, and (c) comparison between
the phase diagram generated using the Schröder–van Laar
(SVL) equation model and DSC study.
(a) Overlaid
DSC thermograms of the APAP/CAFF system, (b) DSC thermogram
of neat APAP as received from the vendor, and (c) comparison between
the phase diagram generated using the Schröder–van Laar
(SVL) equation model and DSC study.
Effect
of the Mixture on the Melting Temperature
of an Individual Component in a Binary System
Shifting or
the depressed melting temperature of the component in the DSC study
indicates the possibilities of interactions between both components
present in the system. In a binary system, if one component (such
as a crystalline drug) is soluble in the molten mass of the second
component at the second component’s melting temperature, then
the system could form a eutectic system. The higher solubility of
the crystalline drug in the eutectic mixture results in either a weak
affinity of the drug molecule to the crystalline solid or a strong
affinity toward the molten mass of the second component.[29,35] IBU/PEG and APAP/CAFF eutectic systems exhibit complete miscibility
in a liquid state and complete immiscibility in the solid state. In
these kinds of binary systems, the liquid phase interaction between
the unlike components is expected to be stronger than that of the
like components.[26] Cooling of the melt
at the eutectic composition leads to the crystallization of both the
phases spontaneously and proceeds with the crystallization of minor
phases in the interstitial spaces of the primary phase.[24,26] According to Tammann’s rule, the lower melting component
tends to be a major phase and the component with a higher melting
point is a minor phase.[36] Therefore, in
IBU/PEG and APAP/CAFF systems, PEG and APAP are major phases, respectively.
During cooling of melts other than at the eutectic composition, only
one component spontaneously starts to crystallize, thereby rendering
the remaining liquor richer in the other component. This was indicated
by the two-melting events in the DSC thermogram at compositions other
than the eutectic composition. The ibuprofen liquidus line for an
ideal binary liquid mixture of IBU/PEG was determined by eq and was observed at a higher temperature
than those determined experimentally. Similarly, in the APAP/CAFF
system, the liquidus lines for caffeine determined by (eq ) were observed at a higher temperature.
This gives a further indication that the minor phase, i.e., ibuprofen
and caffeine, was attractively interacting with the primary phase
PEG and acetaminophen, respectively. The existence of interaction
may be evidenced by the estimation of the fusion excess enthalpy by
applying eq , using
the experimental data shown in Table .where W is the mass fraction of the two components and ΔHf, is the enthalpy of fusion
of the two components.The calculated ΔHf,excess value for IBU/PEG and APAP/CAFF systems is −7.14
and −30.6 J/gm, respectively. In this way, the negative values
of the fusion excess enthalpy of the eutectic mixture indicate the
fine dispersion or the molecular clusters of ibuprofen crystals and
caffeine crystals in the bulk of PEG and acetaminophen, respectively.[24,31,37−39] The nondimensional
fusion entropy (ΔSf°) for the
pure components and respective eutectic mixtures is shown in Table . Fusion entropy was
calculated using the enthalpy of fusion and fusion temperature.[40,41] Components from both the systems have ΔSf° > 2R, which indicates nondimensional
entropy of fusion.[23,24] Fusion entropy data shows that
the eutectic mixtures have higher ΔSf values than the minor crystalline component of the eutectic systems.
This suggests that the eutectic mixture has a higher thermodynamic
state compared to the minor component from IBU/PEG and APAP/CAFF systems.
As reported in the literature, the higher thermodynamic state could
be the manifestation of excessive micronization.[41]
Table 3
Experimental Values of the Thermodynamic
Function of Fusion Enthalpy and Fusion Entropy
sr. no.
component
ΔHf (J/g)
ΔSf (J/(mol K))
ΔSf°/R
1
ibuprofen
130.2
76.9
9.2
2
PEG-6000
179.6
18.3
2.2
3
IBU/PEG (35:65)
155.3
45.1
5.4
4
APAP
178.7
135.02
16.2
5
caffeine
114.2
43.4
5.2
6
APAP/CAFF (60:40)
123.3
82.65
9.9
Powder X-ray Diffraction (PXRD) Studies
In the X-ray diffraction studies, the powder pattern corresponding
to both components in the mixture was assessed by taking reference
powder diffraction patterns of an individual component of the eutectic
system (Figure ).
PXRD pattern shows the crystalline peaks of ibuprofen in the IBU/PEG
system and crystalline peaks for acetaminophen and caffeine in the
APAP/CAFF system (Figure a,b). This illustrates the solid-state stability of one component
in the presence of the second component. However, the crystalline
peaks of neat ibuprofen, acetaminophen, and caffeine were more intense
and sharper compared to the peaks observed in their respective eutectic
mixtures. It was also apparent that the relative intensities of the
observed peak varied, which is in accordance with the published literature,
suggesting that peak broadening could be due to preferred orientation
caused by the growth of anisotropic crystals from a melted sample
and particle size reduction.[42] Similar
results were reported for physical mixtures and solid dispersions
of ketoprofen–PEG-6000 systems in the solid state.[43] Powder pattern of the pure components and eutectic
mixtures in each system superimposed well with individual components.
Although the small changes in the peak intensities were observed,
no change/shifts in peak position indicated the solid-state stability
of ibuprofen with PEG and acetaminophen with caffeine. This supports
the researchers’ idea that the eutectic systems can be formed
by the fusion method without altering the solid-state properties of
the individual component.
Figure 3
(a) Overlaid powder pattern of components from
the IBU/PEG system.
(b) Overlaid powder pattern of components from the APAP/CAFF system.
Figure 4
(a) Particle size distribution (PSD) of components from
the IBU/PEG
system. (b) Particle size distribution of components from the APAP/CAFF
system.
(a) Overlaid powder pattern of components from
the IBU/PEG system.
(b) Overlaid powder pattern of components from the APAP/CAFF system.(a) Particle size distribution (PSD) of components from
the IBU/PEG
system. (b) Particle size distribution of components from the APAP/CAFF
system.
Particle
Size Distribution Studies
The solidified material of both
eutectic systems was grounded further
before subjecting to dissolution studies. To eliminate or lower the
influence of variation in particle size in dissolution, particles
with similar particle size distribution (PSD) were selected for dissolution
analysis. The PM and FM from the IBU/PEG system showed unimodal PSD
with D50 of 51.9 and 51.2 μm, respectively
(Figure a and Table a). Similarly, PM
and FM from the APAP/CAFF system showed a unimodal PSD with D50 of 23.5 and 19 μm, respectively (Figure b and Table b). The PM and FM with a particle
size less than 100 μm were compressed to form a compact using
Wood’s apparatus.
Table 4
Particle Size Distribution
Data of
Components from (a) the IBU/PEG System and (b) the APAP/CAFF System
(a)
sample name
D10 (μm)
D50 (μm)
D90 (μm)
ibuprofen
18.10
59.60
140.00
PEG-6000
11.60
45.60
122.00
PM of IBU/PEG
14.20
51.90
126.00
FM of IBU/PEG
14.30
51.20
134.00
Effect
of Eutectic Temperature on the Theoretical
Solubility of Drugs
Forming a eutectic system of a poorly
soluble compound is touted as one of the alternatives to improve its
solubility in an aqueous medium. The solid dispersion of poorly soluble
drugs in a hydrophilic matrix has been reported to improve the solubility
and dissolution rate. The eutectic composition has a lower melting
point than that of either of the pure components. So theoretically,
lowering the melting point might be expected to result in increased
solubility. However, the thermodynamic counter-argument hypothesized
demanded testing. To test this hypothesis, the solubility of ibuprofen
in the IBU/PEG system and acetaminophen and caffeine solubility in
the APAP/CAFF system was estimated from the theory using drugs’
melting temperature (TM) vs the eutectic
temperature (TE) of the system (eq ).where R is the gas constant,
ΔHfusion is the enthalpy of fusion
of the pure component, Tdiss is the temperature
at which the solubility or dissolution test is performed, TM or TE is the measured
melting temperature of the pure component or eutectic temperature
of the system, and X is the mole fraction of the
component.Assuming the same activity coefficient, the theoretical
solubility of ibuprofen, acetaminophen, and caffeine was calculated
using the dissolution system temperature of 37 °C, the TE of the respective binary system, and the TM of the pure component(s) (Table ). Based on the calculation,
ibuprofen has a theoretical solubility using TE of 25.34 mg/mL and using the TM of ibuprofen is 12.68 mg/mL. This predicts that forming an ibuprofen
eutectic with PEG should increase drugs’ solubility approximately
by 2-fold if TE is, in fact, the controlling
quantity. Similar results were found with the APAP/CAFF system. The
solubility at 37 °C of acetaminophen at TE is calculated to be 0.57 mg/mL and at TM of acetaminophen is 0.12 mg/mL. While the solubility of caffeine
at TE is 10.05 mg/mL and at TM of caffeine is 2.55 mg/mL. Therefore, according to the
estimates, the eutectic of APAP/CAFF should exhibit an increase in
the solubility of the individual components approximately by 3.5-fold.
This predicts that the dissolution rate of ibuprofen in IBU/PEG and
acetaminophen, caffeine in the APAP/CAFF system at the eutectic composition
should be higher by some proportional amount. These results were compared
with the in vitro dissolution testing data to test the hypothesis.
Table 5
Experimental Data Used for the Theoretical
Solubility Calculation of Individual Components from a Binary System
temperature
of (K)
component
heat of fusion (kJ/mol)
melting of
neat drug
melting of eutectic mix
dissolution test performed
ibuprofen
26.82
348.75
322.06
310.15
APAP
59.74
442.45
404.61
310.15
caffeine
22.17
510.53
404.61
310.15
In Vitro
Dissolution Studies
Both
binary systems were tested for their dissolution performance, as described
in the methods section. Per USP, pH 7.2 phosphate buffer was the dissolution
media to test the solubility/dissolution performance of ibuprofens.
At pH 7.2, ibuprofen dissociates very rapidly, which, in turn, increases
its release rate. This makes it difficult to determine its dissolution
rate constant. Therefore, the authors have selected a dissolution
medium in which ibuprofen remains unionized during dissolution, which
helps in estimating the dissolution rate constant. However, ibuprofen-free
acid has poor aqueous solubility and wettability, which limits the
solubility in pH 1.2, so acetonitrile was used as a cosolvent in the
dissolution medium to increase its solubility. Wood’s apparatus
for measuring intrinsic dissolution was used to provide a more objective
data set for comparing the dissolution behavior of the physical mixtures,
a fused mixture, and neat drugs.After an initial 5 min of dissolution
run, the compact of IBU/PEG in Wood’s apparatus showed an uneven
surface, indicating a change in the surface area (Figure a). However, in the case of
neat drugs, the surface was intact for a longer time and showed a
linear relationship between drug release and time (Figure b). However, for comparison
purposes of PM and FM, only the first 5 min data was considered to
calculate the dissolution rate constant. However, the complete profile
was compared to demonstrate the percent cumulative release of drugs
from PM, FM, and neat drugs.
Figure 5
(a) Photograph of Wood’s apparatus in
dissolution media
showing the uneven surface of the IBU/PEG powder compact. (b) Photograph
of Wood’s apparatus in dissolution media showing the intact
surface of the neat ibuprofen powder compact.
(a) Photograph of Wood’s apparatus in
dissolution media
showing the uneven surface of the IBU/PEG powder compact. (b) Photograph
of Wood’s apparatus in dissolution media showing the intact
surface of the neat ibuprofen powder compact.The results showed that the dissolution rate of ibuprofen from
PM and FM increased markedly as compared to the drug alone. However,
the dissolution rate from the FM was no higher than the PM. This is
in contrary to the literature, supporting the claim of an increase
in the dissolution rate of the drug due to its incorporation into
a eutectic mixture as well as the estimated solubility calculation
using the eutectic temperature as the controlling fusion event. In
fact, the dissolution rates from the PM and FM showed similar dissolution
rates, i.e., 1.623 and 1.663 mg/(cm2 min), respectively
(Figure a). Both mixtures
showed a 100% ibuprofen release in approximately 15 min, however the
drug alone took a much longer time (Figure b). The drug alone showed much slower dissolution
compared to PM and FM, i.e., 0.540 mg/(cm2 min) (Table a) due to the absence
of the hydrophilic PEG, which constitutes up to 65% (w/w) of the binary
mixtures. The presence of PEG in the system improves the drug’s
wetting by the dissolution medium and can act locally as a cosolvent,
which could result in an increased dissolution compared to the drug
only. If so, then ibuprofen dissolution should and was observed to
increase by making a physical mixture of ibuprofen with PEG without
making a fused mixture. This indicates that in the IBU/PEG system,
it is not the eutectic, but the presence of PEG causing the increase
in the dissolution rate. This supports the hypothesis that if crystal
lattice energy is not changed in the eutectic mixture, then the solubility
and dissolution study results from FM will be comparable to the results
from the PM, all else being equal.
Figure 6
(a) Intrinsic dissolution plot of neat
ibuprofen, IBU from PM and
FM of the IBU/PEG mixture; (b) % cumulative amount dissolved profile
of neat ibuprofen, IBU from PM and FM of the IBU/PEG mixture in 0.1
M HCl with acetonitrile (30% v/v).
Table 6
Dissolution Rate of (a) the IBU/PEG
System; (b) APAP in the APAP/CAFF System; and (c) CAFF in the APAP/CAFF
System
(a)
sr. no.
sample name
dissolution rate (mg/(cm2 min)) ± SD
1
ibuprofen
0.540 ± 0.014
2
IBU from PM of IBU/PEG
1.623 ± 0.278
3
IBU from FM of IBU/PEG
1.663 ± 0.447
(a) Intrinsic dissolution plot of neat
ibuprofen, IBU from PM and
FM of the IBU/PEG mixture; (b) % cumulative amount dissolved profile
of neat ibuprofen, IBU from PM and FM of the IBU/PEG mixture in 0.1
M HCl with acetonitrile (30% v/v).Further, a eutectic
was formed in the absence of a solubilizing
compound (e.g., PEG). A second binary mixture of acetaminophen and
caffeine (APAP/CAFF) system was selected and its dissolution performance
was studied. As mentioned earlier, because of the powder incompressibility
issue, intrinsic dissolution was not a choice. Therefore, tablet dissolution
was further used to study the effect of the eutectic mixture on the
dissolution performance of a binary mixture of APAP/CAFF. PM and FM
mixtures were blended with 66% (w/w) silicified microcrystalline cellulose
(SMCC) and compressed such that hardness of the tablets ranged between
14 and 16 kPa. Figure shows the dissolution profile of the APAP/CAFF system. The dissolution
rates of APAP and CAFF in PM and FM were approximately similar, showing
no significant difference in the dissolution rate between FM and PM
(Table b,4c). This demonstrates that the eutectic formation
of APAP/CAFF did not drastically improve the dissolution rate, so
the solubility as compared to PM. This supports the observations from
the IBU/PEG system that if crystal lattice energy was unchanged and
local contact between the components kept constant in FM and PM, then
solubility and dissolution results should not differ significantly.
Figure 7
(a) Dissolution
profile of neat acetaminophen, APAP from PM and
FM of the APAP/CAFF mixture in deionized water. (b) Dissolution profile
of neat caffeine, CAFF from PM and FM of the APAP/CAFF mixture in
deionized water.
(a) Dissolution
profile of neat acetaminophen, APAP from PM and
FM of the APAP/CAFF mixture in deionized water. (b) Dissolution profile
of neat caffeine, CAFF from PM and FM of the APAP/CAFF mixture in
deionized water.Different thermodynamic
models are published in the literature
to determine the ideal or real solubility of the compound. These models
include the van’t Hoff equation and ideal models. Based on
the ideal model, if the solution is ideal, then the solubility of
the compound can be calculated using eq , where the effect of the activity coefficient was
considered as negligible.where R is the gas constant,
ΔHfusion is the enthalpy of fusion
of the pure component, T is the temperature at which
the solubility test is performed, TM is
the measured melting temperature of the pure component, and X is the mole fraction of the component.However,
most often the resulting solutions are nonideal and the
activity coefficient ln(γ) plays a major role in determining
the real solubility of the compound in a given media. Therefore, on
the basis of the activity coefficient method, the equilibrium solubility
of the compound may be expressed by the simplified equation (eq ).Based on the simplified
real solubility expression (eq ), an improvement in dissolution
or the solubility of the drug compound in its eutectic mixture is
entirely dependent on the factors of the activity coefficient in the
medium and the crystal lattice (energy and melting point).[44] So, if crystal lattice energy is unchanged in
the eutectic and improvement in the dissolution rate is as noted then
all else being equal, enhancements must be because of increase local
contact, i.e., microstructure and/or the solubilizing power of the
other component (e.g., PEG). However, if the local contact is kept
at a constant range, then we should not see any difference in dissolution
or solubility between FM and PM.
Conclusions
Eutectic mixtures have been investigated
for pharmaceutical purposes,
and a number of works claim an increase in solubilization and dissolution
of drug formulation due to the eutectic formation. Based on thermodynamics,
it was hypothesized that the crystal lattice energy of the two components
is unchanged that all else being equal, the dissolution rates of the
eutectic should be the same as a physical mixture. With the combination
of the results obtained from two different binary systems, it may
be concluded that if the crystal lattice energy is not changed in
eutectic mixtures and the local contact between both the components
is kept constant, then a physical mixture (PM) and a fused mixture
(FM) of the same components will yield similar dissolution profiles.The results show that the presence of a hydrophilic compound as
one of the components in a physical or fused mixture will tend to
increase the dissolution rate of a poorly soluble drug by solubilizing
the drug during dissolution, making it appears as if the increase
is related to the eutectic. PXRD studies showed that the crystalline
pattern crystallinity of the target analyte is not changed; however,
lower peak intensities have been noted, which could be due to the
preferred orientation, masking effect by the second component from
the binary mixture and/or some disorder in the crystalline components.A theoretical calculation using the eutectic melting point instead
of the drug’s melting point showed a 3–4-fold increase
in drug’s predicted solubility and therefore the intrinsic
dissolution rate. However, the data show that the release from the
FM did not improve the dissolution of IBU/PEG or APAP/CAFF when compared
with their respective PM’s dissolution profiles. The hypothesized
explanation is that the unchanged crystal lattice energy in eutectics
limits the solubility (and therefore dissolution rate) is consistent
with the results being substantially the same. As discussed, using
the simplified real solubility expression (eqs and 5b) change in dissolution
so the solubility of the drug in the eutectic mixture is dependent
on two major factors, which are the activity coefficient of the media
and crystal lattice (energy and melting point). This leads to the
conclusion that if there is no change in the crystal lattice energy
and the local contact is kept at a constant range, then FM and PM
will have the same dissolution rate.
Experimental
Section
Materials
Ibuprofen (IBU), acetaminophen
(APAP), and caffeine (CAFF) were obtained from Fagron Inc. Poly(ethylene
glycol) (PEG-6000 PF) was purchased from Clariant. Silicified microcrystalline
cellulose (Prosolv SMCC-HD 90) was obtained from JRS Pharma. All materials
were of pharmaceutical or analytical grade as appropriate. Deionized
water was generated in-house using the Sigma-Millipore system.
Preparation of Solid Dispersion
Solid
dispersions of ibuprofen (IBU) with poly(ethylene glycol) (PEG-6000
PF) and acetaminophen (APAP) with caffeine (CAFF) were prepared by
the fusion method. Approximately, 1000 mg of the physical mixture
(PM) of IBU/PEG and APAP/CAFF was prepared by geometric mixing. Each
mixture was placed in a glass vial, which was immersed in mineral
oil and heated at 80 °C (for IBU/PEG) and 240 °C (for APAP/CAFF).
The fused mixture was stirred to ensure complete mixing and then allowed
to cool to room temperature keeping undisturbed. The solidified material
was gently grounded with a mortar pestle and size fractions were separated
through the nest of sieves. Particles having a size <100 μm
were collected and used for further studies. Grounded materials were
stored in a desiccator containing drierite (anhydrous calcium sulfate)
for approximately 24 h before analysis.
Generation
of the Eutectic Phase Diagram by
Differential Scanning Calorimetry (DSC)
The eutectic phase
diagrams were constructed using the data obtained from differential
scanning calorimetry (DSC). The grounded solidified material (5.0
± 0.2 mg) from each fused mixture was weighed in Tzero aluminum
DSC pans. The pans were nonhermetically sealed and subjected to analysis
using a differential scanning calorimeter (Q2000, TA Instruments).
Before the sample analysis, indium was used to calibrate DSC for the
baseline, temperature, and cell constant at a heating rate of 5 °C/min.
During sample analysis, fused samples were heated at a constant rate
of 5 °C/min and a dry nitrogen purge was maintained at 50 mL/min.
Each mixture of IBU/PEG and APAP/CAFF was heated from 20 to 100 °C
and 20 to 250 °C, respectively. The results were analyzed using
the Universal Analysis 2000 software (TA Instruments, New Castle,
DE).
Powder X-ray Diffraction (PXRD)
PXRD
patterns of the samples were recorded at room temperature (25.0 ±
2.0 °C) on a Smartlab scanning diffractometer (Rigaku Corporation,
Tokyo, Japan) using copper Kα radiation with a potential of
44 kV and 40 mA power. The analysis was performed in a continuous
mode with a scan rate of 0.2°/min over an angular range of 5–35°
2θ. Obtained diffractograms were analyzed with the PDXL-2 diffraction
software (Rigaku Data Analysis Software). Data was used to determine
any possible changes in the crystalline patterns of ibuprofen, acetaminophen,
and caffeine in respective binary mixtures.
Particle
Size Distribution (PSD)
Particle size distributions were
determined using a laser diffraction
particle size analyzer (Mastersizer 3000, Malvern Instruments, Westborough).
Binary mixtures at eutectic composition, ibuprofen, PEG-3000, acetaminophen,
and caffeine were tested for particle size analysis. Approximately,
0.5 ± 0.1 g of the sample was used for particle size analysis.
Reported data of D10, D50, and D90 were the mean
of the triplicate study.
Dissolution Studies
Powdered samples
of IBU/PEG at their eutectic composition were compressed at 88 MPa
using the Wood’s die using a Carver press. The Wood’s
apparatus containing the compressed powdered sample or tablet of the
fused mixture made from the fusion method, physical mixture, and neat
drugs was tested for dissolution performance using USP dissolution
apparatus type II (Symphony 7100/Opt-Diss 410, Distek Inc., NJ) at
a speed of 50 rpm and a temperature of 37 ± 0.2 °C. The
dissolution performance of the IBU/PEG system was tested in 0.1 M
HCl with acetonitrile (30% v/v), and a single wavelength calculation
method was used to calculate the % ibuprofen release. However, APAP/CAFF
was not compressible in the Wood’s die; therefore, dissolution
performance was tested using tablet dissolution. Because of powder
incompressibility, silicified microcrystalline cellulose (SMCC) was
used to improve the compressibility of APAP/CAFF. Each tablet containing
66% of SMCC and 34% of APAP/CAFF was compressed between 150 and 200
MPa to achieve a target tablet hardness of 15 kPa. Deionized water
was used as a dissolution media to test dissolution performance of
APAP/CAFF tablets. The multicomponent method was selected to determine
the % release of APAP and CAFF from the mixtures. The standard solution
of the individual active pharmaceutical ingredient was prepared separately
by dissolving in respective dissolution media and scanned through
a wavelength of 200–400 nm to determine the λmax.