Shubhangi Kakkar1, Lai Zeng2, Michael Svärd2, Åke C Rasmuson1,2. 1. SSPC, Bernal Institute, Department of Chemical Sciences, University of Limerick, Limerick V94 T9PX, Ireland. 2. Department of Chemical Engineering, KTH Royal Institute of Technology, Stockholm SE-100 44, Sweden.
Abstract
A new polymorph of the drug active pharmaceutical ingredient piracetam (Form VI) has been discovered and characterized by X-ray powder diffraction (PXRD), solid-state Raman, attenuated total reflectance infrared spectroscopy, and differential scanning calorimetry. The PXRD diffractogram of Form VI shows a distinct peak at 24.2° (2θ) that distinguishes it from the previously known polymorphs and solvates. Form VI is metastable with respect to the previously known polymorphs Form II and Form III; in ethanol solution at 288 K, Form VI transforms into Form II within 15 min, while in isopropanol solution Form VI is kinetically stable for at least 6 h. A total of 1200 crystal nucleation induction time experiments of piracetam in ethanol and isopropanol solutions have been conducted, in sets of 40-80 repeat experiments carried out at different temperatures and solute concentrations. Each solution nucleated as a single polymorph, and each set of repeat experiments resulted in different proportions of Form II, Form III, and Form VI, with Form VI dominating at low nucleation temperatures and Form II at higher nucleation temperatures. The induction time data for Form VI at 288 K have been evaluated within the framework of the classical nucleation theory. At equal driving force, nucleation of Form VI is less obstructed in ethanol than in isopropanol, as captured by a lower interfacial energy and higher pre-exponential factor in ethanol. The proportion of Form VI obtained at a comparable driving force increases in the order ethanol < isopropanol.
A new polymorph of the drug active pharmaceutical ingredient piracetam (Form VI) has been discovered and characterized by X-ray powder diffraction (PXRD), solid-state Raman, attenuated total reflectance infrared spectroscopy, and differential scanning calorimetry. The PXRD diffractogram of Form VI shows a distinct peak at 24.2° (2θ) that distinguishes it from the previously known polymorphs and solvates. Form VI is metastable with respect to the previously known polymorphs Form II and Form III; in ethanol solution at 288 K, Form VI transforms into Form II within 15 min, while in isopropanol solution Form VI is kinetically stable for at least 6 h. A total of 1200 crystal nucleation induction time experiments of piracetam in ethanol and isopropanol solutions have been conducted, in sets of 40-80 repeat experiments carried out at different temperatures and solute concentrations. Each solution nucleated as a single polymorph, and each set of repeat experiments resulted in different proportions of Form II, Form III, and Form VI, with Form VI dominating at low nucleation temperatures and Form II at higher nucleation temperatures. The induction time data for Form VI at 288 K have been evaluated within the framework of the classical nucleation theory. At equal driving force, nucleation of Form VI is less obstructed in ethanol than in isopropanol, as captured by a lower interfacial energy and higher pre-exponential factor in ethanol. The proportion of Form VI obtained at a comparable driving force increases in the order ethanol < isopropanol.
Crystallization
from solution is a common unit operation in the
pharmaceutical industry. In crystallization processes, primary nucleation
is of crucial importance for the resulting product properties. The
fundamental mechanisms underlying nucleation are not well understood;
thus, nucleation tends to be unpredictable. Controlling nucleation
is necessary to control particle size, size distribution, and polymorphic
form, which is further affected by many factors, such as temperature
and supersaturation.[1,2] Different solid forms can lead
to variations in product performance, such as solubility, dissolution
rate, or tablet hardness. Polymorphism can lead to dramatic effects
in biological activity between two forms of the same drug. In 1999,
Griesser and Burger reported that out of 953 drug molecules tested,
more than 59% are known to exist in more than one crystal form.[3] During the late 20th and early 21st centuries,
many drugs were recalled[4,5] in the United States
and Europe because of the unexpected appearance of a new polymorph,
e.g., Ritonavir (Norvir) and Rotigotine (Neupro).In polymorphic
systems, the overall effect of the solvent on nucleation
can be very important for the outcome.[6−12] Davey et al. explored the link between supramolecular structuring
in solution and the polymorph nucleating from different solvents,
for the compound 2,6-dihydoxybenzoic acid.[7] Gracin et al.[13] in a study of p-aminobenzoic acid, an enantiotropic polymorphic system,
showed that the influence of the solvent on nucleation could be explained
by analyzing the crystal structure and the possible solute–solvent
interactions in the solution. Chiarella et al.[14] in another nucleation study of inosine with a combination
of computational and experimental tools explored the relationship
between the solution-phase inosine species and the structural synthons
present in its crystal structures. Overall, the mechanisms behind
the influence of the solvent are insufficiently understood, and the
polymorphic outcome cannot be predicted. Thus, more studies are required
to understand these mechanisms, which can differ greatly between different
systems.Piracetam (PCM, 2-(2-oxopyrrolidin-1-yl)-acetamide),
shown in Figure ,
is a nootropic
agent used for memory enhancement in humans. Piracetam is approved
in many European countries for myoclonus and aging-related conditions
like Alzheimer’s disease. It is an effective drug for memory
dysfunction, alcoholism, Raynaud’s phenomenon, deep vein thrombosis
(DVT), stroke, tardive dyskinesia, dyslexia, brain injury, and vertigo.
Previously five polymorphic forms of piracetam have been reported,
but two of these (Form IV (8.954) and Form V (6.390)) have only been
obtained at high-pressure (>0.5 GPa) conditions.[15] The remaining three polymorphs (Form I (6.747), Form II
(6.403), and Form III (6.525)) have been identified and structurally
characterized under ambient conditions.[16] For clarity, the numbers within parentheses refer to the unit cell
dimension along the A-axis in Å. The trimorphic thermodynamic
stability relationship is rather complex, which despite being well-studied
is not completely elucidated.[17] Out of
the three polymorphs, Form I is unstable below 383.15 K and can be
isolated only by heating Form II or Form III to 400 K and then quenching
to room temperature, which however typically leads to transformation
back to Form II within a few hours. Form I is thus not of much practical
relevance. At ambient temperature, Form II is metastable, and Form
III is the stable polymorph. Form I and Form III are enantiotropically
related, with a reported transition temperature at 393 K.[17] The solubilities of Form II and Form III have
been determined in a range of organic solvents[18,19] together with an investigation into the polymorphic transformation
behavior. These studies have shown that there is no transition in
stability between these two polymorphs over the temperature range
278–323 K. Kuhnert-Brandstatter et al.[20] have proposed that all three polymorphs are enantiotropically interrelated,
with Form II and Form III having a transition temperature greater
than 348.15 K, but because both forms tend to transform to FI at high
temperatures, there is only indirect experimental evidence for the
existence of such a transition temperature.[17] In addition to the ansolvate forms, crystallization experiments
in water have revealed the existence of a monohydrate form[15] of piracetam, as well as a dihydrate form[21] that has however only been obtained at high
pressure.
Figure 1
Two-dimensional structure of piracetam (2-(2-oxopyrrolidin-1-yl)-acetamide).
Two-dimensional structure of piracetam (2-(2-oxopyrrolidin-1-yl)-acetamide).Various analytical techniques like powder X-ray
diffraction (PXRD), in situ energy dispersive X-ray
diffraction, in
situ Raman spectroscopy, infrared spectroscopy (IR), and
near-infrared spectroscopy have been used to investigate the solid-state,
solution-mediated, and wet granulation-induced polymorphic transformations
of piracetam.[17,20,22−27] Recently, our group published a detailed study on the crystal growth
kinetics of the metastable Form II and the stable Form III in two
organic solvents.[28] However, to the best
of our knowledge, no crystal nucleation induction time study of piracetam
has been reported so far .During preliminary nucleation experiments
in ethanol and isopropanol,
a new crystal polymorph (Form VI) was encountered. The new Form VI
has been characterized using X-ray powder diffraction (PXRD), Raman
spectroscopy, attenuated total reflectance infrared spectroscopy (ATR-IR),
and differential scanning calorimetry (DSC). A total of 1200 isothermal
nucleation induction time experiments have been performed under different
conditions of temperature and concentration, resulting in Form VI
nucleating in the majority of cases. The solubility of Form VI has
been determined by a gravimetric method, and the nucleation parameters
of the new polymorph were determined in ethanol and isopropanol.
Experimental Section
Materials
Piracetam (PCM Form III,
2-(2-oxopyrrolidin-1-yl)-acetamide, 99.9% wt., CAS number 7491-74-9)
was supplied by Baoji Guokang Bio-Technology Co., Ltd., Baoji, China,
complying with European Pharmacopoeia standards EP 6.0. The solvents
used were ethanol (EtOH, 99.8% GC, CAS number: 64-17-5), and isopropanol
(IPrOH, 99.98%GC, CAS number: 67-63-0), both supplied by Fisher Scientific
Ltd. All chemicals were used as received without further purification.
Polymorph Characterization
PXRD,
solid-state Raman spectroscopy, differential scanning calorimetry
(DSC), and ATR-IR have been used to characterize Form III (as received),
Form II, and Form VI (obtained in nucleation experiments). Crystals
of the three polymorphs have also been characterized using optical
microscopy (Olympus XI53) and scanning electron microscopy (JEOL JCM-5700).
Transmission powder X-ray diffractograms were recorded using an Empyrean
diffractometer (Malvern PANalytical Ltd..) with Cu Kα1,2 radiation (λ = 1.5406/1.5444 Å) operating at 40 kV and
40 mA at room temperature. Samples were scanned from 13° to 35°
(2θ) with 0.0066° 2θ/min step size and 48.19 s per
step, on a flat stage that was spinning at 4 rpm on transmission mode.
Reflection X-ray powder diffractograms were recorded using an Empyrean
diffractometer (Malvern PANalytical Ltd.) with Cu Kα1,2 radiation (λ = 1.5406 Å) operating at 40 kV and 40 mA
at room temperature. Samples were scanned from 13° to 35°
(2θ) with 0.026° 2θ/min step size and 112.97 s per
step, on a flat stage that was spinning at 4 rpm on reflection mode. Ex situ Raman spectroscopy was performed using a probe Mettler
Toledo spectrometer. For each spectrum, five scans were collected
for 30 s each from 4000 to 100 cm–1 at 1 cm–1 resolution using iCRaman software v4.3. Ex
situ infrared spectroscopy was performed using a PerkinElmer
Spectrum One spectrophotometer with an ATR accessory equipped with
a ZnSe sample plate. For each spectrum, four scans were collected
from 4000 to 650 cm–1 at a resolution of 4 cm–1. DSC was performed using a Netzsch Polyma DSC 214
instrument, with Concavus Al pans with pierced lids. All runs were
performed at a heating rate of 10 K min–1 heating
rate, from 293 K to 443 K.
Induction Time Experiments
Initially,
240 induction time experiments (Set I) were carried out at different
solute concentrations and temperatures in the range 283.15–298.15
K in ethanol only, with 40 repeat experiments at each condition. The
concentration and temperature combinations were selected somewhat
arbitrarily, with the primary goal to find a suitable basis for an
investigation into the kinetics of nucleation of piracetam. A further
960 induction time experiments (Set II) were then carried out at 288.15
K in ethanol and isopropanol, with 80 repeat experiments at each condition,
to estimate the interfacial energy, pre-exponential factor, and solubility
of the new polymorph.An agitation rate of 200 rpm was used
in all the experiments. Temperature control and agitation were achieved
using thermostatic water baths (Grant, GR150-S26 stirred with pump
and a C2G cooling unit) equipped with submersible multipole magnetic
stirrer plates. The experiments were carried out in batches of 40
simultaneous induction time experiments, in glass vials (VWR, 70.5
× 27.5 mm). Two water baths, each with a submersible 20-pole
magnetic stirrer plate, were set at the nucleation temperature, and
one water bath with a submersible 40-pole magnetic stirrer plate was
used for dissolution. For the nucleation experiments, all the 40 vials
were moved from the high-temperature water bath to the low-temperature
water baths (20 vials in each bath). The vials were recorded using
a high-definition camcorder (Sony HDRXR520VE). The visible onset of
nucleation was characterized by sharp transition from a clear to a
completely opaque solution within 5–10 s. The induction time
was taken as the time interval between the insertion of a vial into
the bath at the nucleation temperature and the first change noticed
in the sample, as observed by the naked eye from the camcorder recordings.
As soon as each specific vial had visibly nucleated, the suspension
was filtered within ∼2 min using a filter paper (Whatman),
and the solids were dried on the filter paper at room temperature
for 24–72 h in a laboratory fume hood to complete dryness.
The samples were then analyzed for the polymorphic form using PXRD
and Raman spectroscopy, with the dried powder samples used directly
with only light or no grinding to avoid polymorphic transformation.
From some vials, only half of the sample was filtered, and the remaining
5 mL was analyzed after ∼15 min to investigate if polymorphic
transformation had occurred.A reference vial, stirred, containing
only the solvent and an in situ temperature probe
(Dostmann model number P600) was
placed in the bath at the nucleation temperature along with the other
vials, in order to determine the time for the solution in a vial to
reach the nucleation temperature. A total of 260–315 s was
required to reach the nucleation temperature to within ±0.5 K,
and 385–425 s to reach the nucleation temperature to within
±0.1 K.
Set I
Solutions of piracetam (starting
with Form III) using selected concentrations were prepared in two
glass bottles (sealed using plastic screw caps) with a 200 mL stock
solution in each bottle. The stock solutions were agitated with PTFE-coated
magnetic stir bars and equilibrated for 4 h at a temperature 5 K above
the temperature corresponding to saturation with respect to Form III.[18] From the respective stock solution, 10 mL aliquots
were filtered into 40 vials using preheated syringes and 0.2 μm
PTFE filters (Millipore), taking care not to induce nucleation during
the preparation and maintaining solution temperatures above the respective
saturation temperature. To each vial, a magnetic stir bar (Sigma-Aldrich,
polygon-shaped, 1/2 × 1/8 in.) was added before sealing with
a plastic screw cap with a PTFE seal. After sealing, the vials were
equilibrated overnight (∼16 h) under agitation at 5 K above
the Form III saturation temperature, before being transferred to the
nucleation baths.
Set II
For the
second set of experiments
(Set II), stock solutions of PCM were prepared in six different concentrations
each in ethanol and isopropanol. From each of the stock solutions,
20 mL samples were filtered into 80 glass vials using the procedure
and equipment specifications described in section . As for Set I, the capped vials were
equilibrated overnight (∼16 h) under agitation at 5 K above
the saturation temperature, before being transferred to the nucleation
baths.
Solubility Measurement
An estimate
of the solubility of Form VI in ethanol and isopropanol at 288.15
K was obtained using a previously described[29,30] gravimetric procedure. In the present work, equilibrium was reached
by nucleation and growth rather than by dissolution. Following nucleation,
2 mL solution samples were extracted from the vials at intervals of
2 min, starting from the point when the solutions turned cloudy. To
facilitate solid–liquid separation, stirring was switched off,
and liquid samples were collected from the clear solution at the top.
Samples of the solid phase present were also collected and analyzed
with PXRD to verify the polymorphic form. Within 8 min, the solution
concentration stabilized, and up to this point there was no change
in the PXRD pattern, indicating that no polymorph transformation had
taken place. Transformation from Form VI to Form II was detected 15
min after nucleation in ethanol, as shown in Figure , while no transformation occurred in isopropanol
for at least 6 h. The samples were dried for at least 3 days or until
all solvent had evaporated, as verified by regular recording of the
vial weights. Once dry, the final mass of each vial was recorded,
and the solution concentration in mole fraction was calculated from
the initial and final masses. Solubility values were also converted
to mol L–1 using eq , assuming that the density of the solution can be
approximated by the density of the pure solvent, 0.789 g L–1 for ethanol and 0.785 g L–1 for isopropanol. The
final solubility estimates were taken as the average of three samples
and are reported in Table .
Figure 3
(a–e) Transmission PXRD diffractograms
of dried Form VI
obtained from isopropanol and ethanol immediately after nucleation,
after 6 h for isopropanol and after 15 min in ethanol in stirred suspension
before filtration, compared to PXRD patterns of other polymorphs obtained
from structures in the CSD; Form II: BISMEV, Form III: BISMEV01 Arrows
indicate the characteristic peaks of Form VI.
Table 3
Solid–Liquid Interfacial Energy
(γ), Pre-exponential Factor (A), Solubility
at 288.15 K (g g–1, mol L–1 (C*) and Mole Fraction (x*)) of Form VI,
Solvent Normal Boiling Points, and Pre-Exponential Factor (A/A1) Calculated Using eq from Physical Properties
in Ethanol and Isopropanol
Figure shows the
transmission
PXRD diffractograms of Form VI of piracetam obtained in the present
work by nucleation from ethanol and isopropanol solutions at 298.15
K, together with the theoretical PXRD patterns of Forms I, II, III,
IV, and V, and the reported monohydrate and dihydrate forms, obtained
from structures deposited in the Cambridge Structural Database (CSD).
As shown in Figure , a unique, characteristic peak at a 2θ-value of 24.2°
was observed for the new polymorph. More reflection PXRD graphs obtained
from nucleation experiments for this polymorphic form are shown in
Figure S1 (Supporting Information).
Figure 2
(a–i)
PXRD diffractograms of dried Form VI obtained from
isopropanol and ethanol using the method described in section , compared to PXRD patterns
of other polymorphs obtained from structures in the CSD; Form I:
BISMEV03, Form II: BISMEV, Form III: BISMEV01, Form IV: BISMEV04,
Form V: BISMEV07, monohydrate: YAKWAJ, and dihydrate: LIFNOE. Arrows
indicate the position of a peak distinguishing Form VI from the other
known solid forms.
(a–i)
PXRD diffractograms of dried Form VI obtained from
isopropanol and ethanol using the method described in section , compared to PXRD patterns
of other polymorphs obtained from structures in the CSD; Form I:
BISMEV03, Form II: BISMEV, Form III: BISMEV01, Form IV: BISMEV04,
Form V: BISMEV07, monohydrate: YAKWAJ, and dihydrate: LIFNOE. Arrows
indicate the position of a peak distinguishing Form VI from the other
known solid forms.Figure shows PXRD diffractograms of solids nucleating as
Form VI sampled immediately after nucleation and following additional
time in an agitated suspension, compared with diffractograms of Form
II and Form III obtained using crystal structures available in the
CSD. In ethanol, Form VI is verified to have completely transformed
into Form II after 15 min, but in isopropanol Form VI remains unchanged
for at least 6 h of observation.(a–e) Transmission PXRD diffractograms
of dried Form VI
obtained from isopropanol and ethanol immediately after nucleation,
after 6 h for isopropanol and after 15 min in ethanol in stirred suspension
before filtration, compared to PXRD patterns of other polymorphs obtained
from structures in the CSD; Form II: BISMEV, Form III: BISMEV01 Arrows
indicate the characteristic peaks of Form VI.Figure compares
Raman spectra of different piracetam polymorphs. The spectra obtained
for Form III and Form II match perfectly with spectra already reported
for these forms.[31] Characteristic Raman
shifts of Form III are observed at 843 cm–1, 862
cm–1, 1416 cm–1, and 1438 cm–1, and of Form II at 853 cm–1, 866
cm–1, 1424 cm–1, 1408 cm–1, and 1434 cm–1. Raman shifts of Form VI are observed
at 851 cm–1, 865 cm–1, 1418 cm–1, and 1433 cm–1, differing from
the other polymorphs mainly with respect to the peak at 1418 cm–1 (representing C–H symmetric bending) which
is found at 1408 cm–1 for Form II and at 1438 cm–1 for Form III. The Raman spectrum of Form VI is more
similar to that of Form II than that of Form III. The results obtained
with Raman spectroscopy agree with PXRD in that there is no change
in the solid form obtained from isopropanol solution immediately after
nucleation and after 15 min in suspension, as shown in Figure d. In ethanol suspension, the
Raman spectrum obtained after 15 min indicates a complete transformation
into Form II, as shown in Figure f. Additional solid-state Raman spectra of Form VI
obtained from nucleation are shown in Figure S2 (Supporting Information). The full Raman spectra of all the
forms presented here are shown in Figure S3 (Supporting Information).
Figure 4
Solid-state Raman spectra of (a) Form III as received,
(b) Form
II obtained in this work, and Form VI obtained immediately after nucleation
in (c) isopropanol and (e) ethanol and following a further 6 h and
15 min in stirred suspension in (d) isopropanol and (f) ethanol, respectively.
Arrows indicate the location of the characteristic Raman peak value
distinguishing Form VI from Form II.
Solid-state Raman spectra of (a) Form III as received,
(b) Form
II obtained in this work, and Form VI obtained immediately after nucleation
in (c) isopropanol and (e) ethanol and following a further 6 h and
15 min in stirred suspension in (d) isopropanol and (f) ethanol, respectively.
Arrows indicate the location of the characteristic Raman peak value
distinguishing Form VI from Form II.Figure shows the
ATR infrared spectra of crystals of Form II, Form III, and Form VI.
As for Raman spectroscopy, the three spectra exhibit very small differences.
The main region of distinguishing features between these three polymorphs
is located in the range 1400–1500 cm–1.
Figure 5
ATR FTIR
spectra of (a) Form II obtained in this work, (b) Form
III as received, and (c) Form VI obtained in this work. The region
where differences could be expected to be found between the three
polymorphs is highlighted.
ATR FTIR
spectra of (a) Form II obtained in this work, (b) Form
III as received, and (c) Form VI obtained in this work. The region
where differences could be expected to be found between the three
polymorphs is highlighted.DSC thermograms obtained for the three solid phases (Form II, Form
III, and Form VI; shown in Figure S4 of the Supporting Information) exhibit qualitatively similar behavior; a weak
endothermic transformation peak with an onset between 390 and 400
K, followed by a melting peak with an onset at around 426 K, corresponding
to the reported melting point of Form I.[20,27]The estimated solubility of Form VI in ethanol and isopropanol
at 288.15 K is summarized in Table . In mole fraction terms, the estimated solubility
is higher in ethanol than in isopropanol, in agreement with data reported
for Form II[19] and Form III.[18] At 288.15 K, the solubility ratios in terms
of mole fraction solubility of Form VI: Form II: Form III is 1.195:1.080:1.000
± 0.004 in ethanol and 1.196:1.090:1.000 ± 0.006 in isopropanol.
It should be stressed here that the relative uncertainty in the Form
VI solubility values is higher compared to the Form II and Form III
data because of the difference in method (approaching equilibrium
by nucleation and growth) as well as the short equilibration time
(necessary to avoid transformation).Four samples of the different
polymorphs of piracetam were analyzed
further using optical microscopy and scanning electron microscopy,
shown in Figure and Figure . The samples of
Form II were obtained by crystallization in ethanol and Form VI in
ethanol and isopropanol, while Form III was used as received. The
figures show that the habit of Form III and Form VI (more clearly
seen in samples from isopropanol) is relatively blocky, while the
habit of Form II is more plate-like, for crystals from both solvents.
Figure 6
Optical
micrographs of Form III (as received), Form II, and Form
VI obtained from isopropanol and ethanol.
Figure 7
SEM images
of Form III (as received), Form II, and Form VI obtained
from isopropanol and ethanol.
Optical
micrographs of Form III (as received), Form II, and Form
VI obtained from isopropanol and ethanol.SEM images
of Form III (as received), Form II, and Form VI obtained
from isopropanol and ethanol.
Nucleation
Figure shows the fractions of Set I experiments
resulting in each polymorphic form for ethanol solutions nucleating
at different temperatures and concentrations. In all the Set I experiments,
all 40 vials nucleated within 2.5 h. Moreover, each vial resulted
in a single polymorphic form, i.e., the material in each vial was
polymorphically pure, but different vials were observed to yield different
polymorphs. Samples from each vial were collected by filtering within
5 min of the cloud point being attained in the vial to ensure no further
transformation. The results clearly show changes in experimental conditions
affecting the polymorphic outcome in statistical terms. As the sample
size was relatively small, and as concentrations and temperature combinations
were selected somewhat arbitrarily primarily to find a suitable basis
for the Set II experiments, it is not straightforward to draw clear
conclusions about the influence of individual process conditions.
In the figure, the driving force is given with respect to Form VI,
for 288 K as obtained using the experimentally determined Form VI
solubility, and for other temperatures as calculated from the solubility
of Form III and using the solubility ratio Form VI/Form III at 288.15
K. The driving force is expressed as a chemical potential difference,
Δμ, estimated using eq by approximating activities with concentrations:where TN is the
nucleation temperature, and S is the supersaturation
ratio approximated as the ratio of mole fraction concentrations in
the supersaturated solution (x) and at saturation
(x*). The corresponding driving forces with respect
to Form II and Form III for each experiment can be calculated from
the solubility ratios given above.
Figure 8
Polymorphic outcome of Set I experiments
in ethanol at different
nucleation temperatures and solute concentrations, along with the
nucleation temperature (TN) and nucleation
driving force with respect to Form VI. The fraction of vials (%) nucleated
as each respective polymorph are given as numerical values, and error
bars show 95% confidence limits calculated using the Wilson method[32] with no correction for continuity.
Polymorphic outcome of Set I experiments
in ethanol at different
nucleation temperatures and solute concentrations, along with the
nucleation temperature (TN) and nucleation
driving force with respect to Form VI. The fraction of vials (%) nucleated
as each respective polymorph are given as numerical values, and error
bars show 95% confidence limits calculated using the Wilson method[32] with no correction for continuity.In order to evaluate the nucleation kinetics of Form VI, a low
nucleation temperature (288.15 K) was chosen for a second set (Set
II) of induction time experiments in ethanol and isopropanol solutions.
In Set II, all 80 vials nucleated within the experimental time frame,
and each set of repeat experiments resulted in proportions of vials
each nucleating as a single polymorph. The polymorphic outcome is
given in Table . All
conditions resulted in the majority of vials nucleating as Form VI:
> 83% of the vials in ethanol and >88% in isopropanol.
Table 1
Polymorphic
Outcome of Eighty Vials
Nucleated in Set II Experiments Carried out at Different Driving Forces
for Nucleation (with Respect to Form VI):
ethanol
Δμ (kJ mol–1)
1.40
1.46
1.51
1.61
1.67
1.72
Form VI
69 (86.2%)
68 (85.0%)
68 (85.0%)
67 (83.8%)
66 (82.5%)
66 (82.5%)
Form II
11 (13.8%)
12
(15.0%)
12 (15.0%)
13 (16.2%)
12 (15.0%)
10 (12.5%)
Form
III
2 (2.5%)
4 (5.0%)
Figure shows the
fractions of Set II experiments resulting in each polymorph for different
supersaturation values. The supersaturation is quantified as the thermodynamic
driving force for nucleation of Form VI, given by eq , and using the experimentally determined
mole fraction solubility (x* in Table ) of Form VI at 288.15 K. In
both solvents, there is a weak but consistent trend showing a larger
proportion of vials nucleating as Form VI with decreasing driving
force. In isopropanol, the fraction of vials nucleating as Form II
correspondingly increases with increasing driving force, while in
ethanol the proportion of Form II remains less affected. In ethanol,
some vials nucleate as the stable Form III at higher driving forces,
but this polymorph was not encountered at all in isopropanol. Both
these trends are against expectation, i.e., that the formation of
a more unstable form would be promoted by a higher supersaturation.
However, it should be stressed that these trends cannot be confidently
established within the limits of experimental uncertainty.
Figure 9
Polymorphic
outcomes at different solute concentrations and nucleation
driving forces, at 288.15 K in (left) ethanol and (right) isopropanol
(Set II). The fraction of vials (%) nucleated as each respective polymorph
are given as numerical values, and error bars show 95% confidence
limits calculated using the Wilson method[32] with no correction for continuity.
Polymorphic
outcomes at different solute concentrations and nucleation
driving forces, at 288.15 K in (left) ethanol and (right) isopropanol
(Set II). The fraction of vials (%) nucleated as each respective polymorph
are given as numerical values, and error bars show 95% confidence
limits calculated using the Wilson method[32] with no correction for continuity.The induction time distributions for the experiments nucleating
as Form VI in ethanol and isopropanol at 288.15 K are shown in Figure . Log-normal cumulative
distribution functions are fitted to the experimental data, with overall
good fits (R2 > 0.97) as seen in the
figure.
Figure 10
Induction time distributions of Form VI in (a) ethanol and (b)
isopropanol at a nucleation temperature of 288.15 K at different driving
forces with fitted log-normal cumulative distribution functions (black
solid lines). Each data point represents the induction time obtained
in one single experiment.
Induction time distributions of Form VI in (a) ethanol and (b)
isopropanol at a nucleation temperature of 288.15 K at different driving
forces with fitted log-normal cumulative distribution functions (black
solid lines). Each data point represents the induction time obtained
in one single experiment.The median induction time, extracted directly from the experimental
induction time distributions, for nucleation of Form VI in each experiment
was used as input for further analysis of nucleation parameters. Figure shows a plot of
experimentally obtained median induction times against the driving
force for nucleation of Form VI in ethanol and isopropanol. The median
induction time values are summarized in Table . Median induction time values are calculated
using mole fraction solubilities (x*) mentioned in Table .
Figure 11
Influence of the nucleation driving force on the median induction
time for Form VI in ethanol (blue, ●) and isopropanol (orange,
■), from Set II experiments, together with exponential trend
lines.
Table 2
Median Induction
Times of Form VI
Obtained at Different Driving Forces, at a Nucleation Temperature
of 288.15 K (Set II)
ethanol
Δμ (kJ mol–1)
1.40
1.46
1.51
1.61
1.67
1.72
induction time (s)
2013
1711
1506
1269
1071
986
Influence of the nucleation driving force on the median induction
time for Form VI in ethanol (blue, ●) and isopropanol (orange,
■), from Set II experiments, together with exponential trend
lines.As shown in Figure , in terms of the thermodynamic driving force required,
the barrier
to Form VI nucleation is significantly lower in ethanol than in isopropanol.
The estimated driving force required to reach an induction time of
2000 s (indicated by the dashed line in the figure) is 1.48 kJ mol–1 in ethanol and 1.89 kJ mol–1 in
isopropanol. Thus, for this polymorph, the apparent nucleation difficulty
increases in the order ethanol < isopropanol. However, at the same
time, the proportion of Form VI obtained also increases
in the order ethanol < isopropanol. This indicates that nucleation
of Form II and Form III is even more obstructed in isopropanol compared
to ethanol. In other words, the influence of the solvent on nucleation
appears to be more pronounced for Form II and Form III than for Form
VI.According to the classical nucleation theory (CNT),[33] the rate of nucleation (J)
as a function of S can be expressed aswhere TN (K) is the nucleation temperature, A (m–3s–1) is the pre-exponential
factor,
and S is the supersaturation ratio. Assuming the
induction time to be equal to 1/JV:where τ50 denotes the median
induction time, extracted directly from the experimental induction
time distributions, and V is the solution volume
(20 mL). Figure shows classical nucleation plots of ln(τ50S) against ln–2S·TN–3 for nucleation in both solvents.
The pre-exponential factor (A) value is calculated
from the intercept, and the interfacial energy (γ) is further
calculated from the slope B through the equation:where k (J·K–1) is the Boltzmann constant,
and ϑ (m3) is the molecular
volume. For all the calculations, the molecular volume of piracetam
was taken as that in the crystal structure of Form II (CSD refcode
BISMEV) equal to 1.74 × 10–28 m3. The values of the pre-exponential factor and the interfacial energy
are given in Figure . The easier nucleation in ethanol is reflected in both a lower interfacial
energy and a higher pre-exponential factor.
Figure 12
Classical nucleation
plot of Form VI in ethanol (blue, ●)
and isopropanol (orange, ■), together with respective linear
correlations.
Classical nucleation
plot of Form VI in ethanol (blue, ●)
and isopropanol (orange, ■), together with respective linear
correlations.
Discussion
As the comparison of PXRD patterns shows (Figure ), Form VI is a new polymorphic form of piracetam.
The structural changes that occur over time clarify that this polymorphic
form is less stable than both Form II and Form III under ambient conditions.
The stability relationship is also evident from a comparison of the
solubility of the three forms in the same solvents. At 288 K, the
estimated solubility of Form VI (0.0311 g g–1 in
EtOH and 0.0143 g g–1 in IPrOH) as shown in Table (C*) is higher than that of Form II[19] (0.0287
g g–1 in EtOH and 0.131 g g–1 in
IPrOH) and of Form III[18] (0.026 g g–1 in ethanol and 0.012 g g–1 in isopropanol).
The transformation of Form VI is slower in isopropanol than in ethanol,
in line with the fact that the solubility in isopropanol is lower.All these three polymorphic forms of piracetam (Form VI, Form II,
and Form III) have been obtained in induction time experiments at
different nucleation temperatures and solute concentrations. It can
be concluded that Form VI is the overall most common result in the
range of conditions evaluated herein. With increased nucleation temperature
and associated higher concentrations, the proportion of experiments
resulting in the more stable polymorphs (Form II and Form III) increases.
This is in general agreement with observations reported for other
systems,[13,34] that with higher concentrations the greater
the tendency to nucleate more stable forms, as a result of an interplay
of thermodynamic and kinetic factors.The driving force required
to reach the same induction time increases
in the order of solvents as ethanol < isopropanol. The estimated
interfacial energy is lower, and the pre-exponential factor is higher
for Form VI in ethanol compared to in isopropanol, as summarized in Table , with both parameters
capturing that nucleation is easier in ethanol. Thus, from both the
above statements, the ease of nucleation of this polymorphic form
of piracetam increases in the order of solvents as isopropanol <
ethanol. Moreover, given the fact that the proportion of Form VI obtained
at equal driving force is higher in isopropanol than in ethanol, nucleation
of Form II and Form III appears even more difficult in isopropanol.A similar order between these two particular solvents has also
been observed for nucleation of n-butyl paraben[35] and fenoxycarb[36] where
the interfacial energy was found to be lower in ethanol compared to
a propanol isomer (n-butyl paraben: 1-propanol and
fenoxycarb: isopropanol). The difficulty of nucleation in isopropanol
can be attributed to the fact that there is a stronger interaction
between the solute and solvent molecules compared to ethanol, as shown
in previous work by Maher et al.[17] using
molecular simulation.In previous works[37] on nucleation of
inorganic compounds in water, an inverse relationship between the
interfacial energy and the natural logarithm of the solubility was
identified. This relationship is also found in the present work for
the two evaluated solvents. However, in several other studies of a
solute nucleating in different solvents, this relationship is not
found.[38−40] As shown in Table , the normal boiling point is higher for isopropanol
compared to ethanol, similar to the order of interfacial energies
of Form VI in the same solvents. A similar relationship has been observed
in other studies,[35,41] while there are also examples
of the opposite.[36,38]In previous work by our
group[28] for
piracetam Form II and Form III in the same solvents, the interfacial
energy calculated from growth experiments was found to be lower in
ethanol (1.12 mJ m–2 Form II; 1.75 mJ m–2 Form III) and higher in isopropanol (1.18 mJ m–2 for Form II; 2.08 mJ m–2 for Form III), the same
order between the solvents as obtained in the present nucleation work
for Form VI (4.15 mJ m–2 in ethanol, 4.45 mJ m–2 in isopropanol). Interfacial energies are expected
to increase with increasing thermodynamic stability of the polymorphic
form. Accordingly, please note that the values for Form II and Form
III are obtained from growth experiments, while the values for Form
VI are from nucleation experiments. Values obtained from growth experiments
are expected to be lower than those determined in nucleation experiments
since in the former type the determination is related to a 2D nucleation
on a crystal face, while the latter is related to a 3D nucleation
in a solution.[42,43]The pre-exponential factor
is dependent on the attachment factor,
the Zeldovich factor, and the concentration of nucleation sites.[40] The attachment factor and the Zeldovich factor
both depend on the interfacial energy. The attachment factor describes
the rate by which molecules attach to the nucleus surface and depends
on the rate of transport to the nucleus and the surface area of the
nucleus. The surface area of the nucleus is governed by the interfacial
energy and the supersaturation. The Zeldovich factor (z) is related to the interfacial energy (γ–3/2). Thus, the pre-exponential factor[33] is
dependent on interfacial energy as per eq :where M (g·mol–1) is the solvent molecular
weight, C* (mol·L–1) is the
solubility obtained in this work as described
in section , and A1 is a proportionality constant
assumed to be independent of the solvent. η (mPa·s) is
the solution viscosity at the nucleation temperature (288.15 K), here
approximated by the solvent viscosity, and ϕ is the empirical parameter used for calculating diffusion coefficient
using the Wilke–Chang equation, whose value is 1 for most solvents
but 1.5 for ethanol.[44] The obtained values
of A/A1 are summarized
in Table . Both this
ratio as well as the experimentally determined pre-exponential factor
values (A) exhibit a higher value in ethanol compared
to isopropanol and thus with respect to the influence of the solvent
show a correlation. Equation indicates that with increasing interfacial energy the pre-exponential
factor would of course be lower, and everything else unchanged. In
the present work, a lower interfacial energy and a higher pre-exponential
factor are found for ethanol solutions of Form VI compared to isopropanol
solutions. Considering the fact that also the viscosity of isopropanol
is higher, it is not surprising that the pre-exponential factor is
lower in this solvent.
Conclusions
A new
metastable polymorph (Form VI) of piracetam has been identified
and characterized using PXRD, solid-state Raman, and IR spectroscopy.
A characteristic peak in PXRD was identified at 24.2° distinguishing
it from other known polymorphs. The new form nucleates preferentially
over other polymorphs in both ethanol and isopropanol under the conditions
investigated, but in ethanol Form VI crystals transform to Form II
within approximately 15 min at 288 K, while in isopropanol the nucleated
Form VI crystals remain unchanged for at least 6 h. At constant supersaturation,
the proportion of experiments resulting in nucleation of Form VI shows
an increasing trend with decreasing temperature of nucleation. Nucleation
of Form VI in ethanol requires a lower thermodynamic driving force
than in isopropanol to reach the same median induction time, the interfacial
energy is lower, and the pre-exponential factor is higher in ethanol.
However, the proportion of experiments nucleating as Form VI is higher
in isopropanol than in ethanol.
Authors: Denise M Croker; Michelle C Hennigan; Anthony Maher; Yun Hu; Alan G Ryder; Benjamin K Hodnett Journal: J Pharm Biomed Anal Date: 2012-01-18 Impact factor: 3.935
Authors: Catherine B Potter; Gayathri Kollamaram; Jacek Zeglinski; Darren A Whitaker; Denise M Croker; Gavin M Walker Journal: Eur J Pharm Biopharm Date: 2017-05-27 Impact factor: 5.571
Authors: Renato A Chiarella; Amy L Gillon; Rebecca C Burton; Roger J Davey; Ghazala Sadiq; Anthony Auffret; Marina Cioffi; Christopher A Hunter Journal: Faraday Discuss Date: 2007 Impact factor: 4.008
Authors: Luciana L DeMatos; Adrian C Williams; Steven W Booth; Catherine R Petts; David J Taylor; Nicholas Blagden Journal: J Pharm Sci Date: 2007-05 Impact factor: 3.534