Formulation and Evaluation
of Solid Dispersion by Novel Technique
Smita
Kolhe1*, Dr. Praveen Chaudhari2, Dhananjay
More3
1P.E.S’s, Modern
College of Pharmacy (For Ladies), Moshi, Pune, Ms, India
2P.E.S’s, Modern
College of Pharmacy, Nigdi, Pune,
Ms, India
3Emcure
Pharmaceuticals Limited, Bhosari, Pune,
Ms, India
*Corresponding Author E-mail: smitamore92@gmail.com
ABSTRACT:
Hot melt extrusion (HME) is the most
widely applied processing techniques, with its several advantages including
enhancement of the dissolution rate and bioavailability, controlling or
modifying drug release, taste masking, stabilizing the active pharmaceutical
ingredient (API). Hot Melt Extruded dosage forms are complex mixtures of API, plastisizers and polymer carriersin
which the molten thermoplastic polymers during the extrusion process can
function as thermal binders and/or release retardants. Present
investigation deals with enhancement of dissolution rate and hence solubility
of Dapsone (Dap). Dap is a primary used for
treatment of Dermatitis herpetiformis, as an
antibacterial drug for susceptible cases of leprosy with long half life of
52-56 hrs. Solubility enhancement techniques are available in wide range but
HME was the preferred technique due to its several advantages. Copovidone (Kollidon VA64) as polymer and polyethylene glycol (PEG
4000), polyoxy 35 castor oil (Cremophor
EL) and sorbiton monolaurate
(Montane 20 PHA) as plasticizers were studied and
optimized. Evaluation techniques like saturation solubility, effect of
temperature on preparation of complexes, differential scanning calorimetry (DSC), x-ray diffraction (XRD), Infra red (IR),
dissolution and in vitro permeability studies were carried out. Results
concluded enhanced dissolution and solubility. Stability studies at 40 º C/75 %
RH (relative humidity)
showed that the sample is
stable even after 3 months study. HME is simple and efficient method to improve
dissolution and permeability of poorly water soluble Dap.
KEYWORDS: Melt extrusion, solubility, glass transition
temperature, plasticizers, BCS class II.
INTRODUCTION:
Dapsone-USP, 4, 4’-diaminodiphenylsulfone (DDS) is
a primary treatment for Dermatitis herpetiformis. It
is an antibacterial drug for susceptible cases of leprosy. Dapsone
is used to control the dermatologic symptoms
of Dermatitis herpetiformis. Dapsone
is used alone or in combination with other anti-leprosy drugs for leprosy.
Biopharmaceutical classification system
(BCS), based on solubility and permeability of drug is divided into four
classes.
Dap shows low aqueous solubility and high
membrane permeability (class II) (1-3)
as per the BCS classification given below:
BCS class I |
BCS class II |
High solubility |
Low Solubility |
High permeability |
High permeability |
BCS Class III |
BCS Class IV |
High solubility |
Low solubility |
Low permeability |
Low permeability |
Increasing dissolution rate of poorly water soluble drug is major challenge in dosage form
development. Bioavailability of orally administered drug mainly depends on its
solubility and permeability. Drug discovery shows that compounds are often high
molecular weight and highly lipophilic hence exhibits
poor solubility.
Dissolution of various drugs can be improved
by (4)
·
Increasing
the surface area available for dissolution.
·
Optimizing
wetting characteristics of compound surface.
·
Decreasing
boundary layer thickness.
·
Ensuring
sink conditions for dissolution.
·
Improve
apparent solubility.
Various solubility enhancement strategies
in solid dispersion are fusion (melting), solvent evaporation, lyophilization (freeze drying), melt agglomeration process,
extruding method, spray drying technique, use of surfactant, electrostatic
spinning method and super critical fluid technology. One approach is formation
of solid dispersion of drug with hydrophilic excipients.
Ideal type of solid dispersion for increasing dissolution requires glass
solution in which amorphous drug has low thermodynamic barrier to dissolve
together with maximally reduced particle size. Also presence of hydrophilic excipients may lead to increase wetting leading to super
saturation in the diffusion layer.
Glass solution is formed when two or more
components are entirely miscible in molten state and cooled to form amorphous
one phase system. For glass solution, melt extrusion studies were preferred due
to several applications and advantages as given below:
Applications include: 5
·
Improving
dissolution rate and bioavailability of drug.
·
Controlling/modifying
release of drug.
·
Masking
bitter taste of drug.
Advantages include: 6
·
Small
equipment
·
Economic
and continuous process and scale up flexibility
·
Solvent
free manufacturing
·
High
mixing efficiency
·
Closed
process unit to prevent cross contamination
·
Short
processing time
·
Easily
controlled process parameters
·
Possibility
of online analytics for process control
Disadvantage includes: 6
·
Thermal
process(drug/polymer stability)
·
Flow
properties of polymers are essential to processing
·
Limited
number of available polymers
·
Require
high energy input
·
Melt
technique process cannot be applied to heat sensitive materials due to high
temperature involved.
HME can be simply
defined as the process of forming a new material (the extrudate)
by forcing it through an orifice or die under controlled conditions, such as
temperature, mixing, feed-rate and pressure. 7
A variety
of carrier systems have been studied or used in HME dosage forms. Such carrier
systems include polyvinylpyrrolidone (PVP) or its
co-polymer such as polyvinylpyrrolidone-vinyl
acetate, copovidone (Kollidon
VA64), poly (ethylene-co-vinyl acetate), various grades of polyethylene
glycols, cellulose ethers and acrylates, various
molecular weight of polyethylene oxides, poly methacrylate derivatives and poloxamers.
Amongst the different classes of biodegradable polymers, the thermoplastic
aliphatic poly (esters) such as poly (lactide) (PLA),
poly (glycolide) (PGA) and copolymer of lactide and glycolide, poly (lactide-co-glycolide) (PLGA) have
been used in extrusion. Starch and starch derivatives have been applied along
with low molecular weight excipients like sugars and
sugar alcohols and waxes.
Plasticizers are added to HME formulations
to facilitate the extrusion of the material and to increase the flexibility of
the extrudate. The choice of suitable plasticizer
depends on many factors, such as plasticizer-polymer compatibility and
plasticizer stability. Polyethylene glycol (PEG 4000), polyoxy
35 castor oil (Cremophor EL) and sorbiton
monolaurate (Montane 20
PHA), triacetin, citrate esters and low molecular
weight polyethylene glycols have been investigated as plasticizers in hot-melt
extruded systems.7-15
Basic requirements for
polymers used in HME:
Ø |
Thermoplastic
behavior |
-deformability
is essential |
Ø |
Suitable Tg |
-50-180ºC |
Ø |
High thermal
stability |
-50-180ºC |
Ø |
Low hygroscopicity |
-prevents
crystallization |
Ø |
No toxicity |
-application of
large amounts possible |
Ø |
High or no solubilisation |
-thermodynamically
stable capability formulation |
MATERIALS AND METHODS:
Dapsone was received as gift sample from Emcure pharmaceuticals limited, Pune,
India. Copovidone (Kollidon
VA64), polyoxyl 35 castor oil (Cremophor EL), PEG 4000, sorbiton monolaurate and all
other reagents and chemicals used were of analytical grade.
METHODS:
1.
Characterisation
of Dap:
Dap was characterized by
following test:
A.
Description:1-3
Dap was studied for its color
and physical appearance.
B.
Saturation Solubility:1
Solubility of Dap was measured
in distilled water. An excess amount of drug was added to 50 ml conical flask
and was kept under shaking for 72 hrs (Rotary shaker, Biomedica).
Saturated solution was filtered through 0.45 µ membrane filter, absorbance of
filtered solutions was determined and amount of drug solubilised
was calculated.
C.
Melting Point: 3,4
Dap melting point was
determined by both the capillary method and instrumental method. Capillary
method was done by taking capillary in which drug was
inserted and then attached to thermometer. Both capillary along with
thermometer was inserted into the parrafin bath which
was heated and the melting temperature was recorded.
Instrumental method involves
insertion of capillary in the paraffin bath and the melting temperature was
recorded electronically (Melting point apparatus VEEGO). This method proved to
be more accurate than the former method.
D.
XRD:12
Dap was subjected to XRD (P.W.
1729, X-ray generator, Philips, Nether land). To study XRD pattern, the drug
sample was placed into aluminum holder and the instrument was operated between
initial and final 2θ angle of 5-500 respectively in an
increment of 0.402θ.
E.
IR:12
Dap, was subjected to Fourier
Transform Infra Red (FTIR 8400s spectrophotometer Shimadzu) studies to check
the characteristic sharp peaks of drug and its functional groups. The Pottasium bromide (KBr) disk
method was used for preparation of sample. The samples were ground gently with
anhydrous KBr and compressed to form pellet. The
scanning range was 400-4000cm-1.
F.
DSC:12
Dap was subjected to DSC study
using (Mettler TA 4000) DSC apparatus. First 5-10 mg
of sample was weighed into aluminum crucible. This powder was analyzed by
heating at scanning rate of 100C / minute over a temperature range
50 to 2000 C with
nitrogen flow of 50mL/min.
2.
Preparation of Calibration Curve:1, 13
100µg/ml stock solution of Dap
was prepared in by first dissolving 100mg of drug in 100mL of 2mL dilute HCl. Further dilutions were done to obtain solutions of
1....10 µg/mL. Respective absorbance values were measured at fixed
λ max.
3.
Determination of Drug :Polymer Ratio:14,15
Solubility of Dap was checked
in different solvents such as methanol, ethanol and water. Both drug and
polymer were soluble in ethanol and hence selected for optimization of ratio.
Drug and polymer (1:1 to 1:5) were solubilised in
ethanol. The obtained solution was then poured in petri
plates and films were cast by solvent evaporation method and were observed
after 24 hrs at room temperature for their appearance.
4.
Effect of Temperature on Decomposition of
Polymers:14,15
Polymer was subjected to
different temperatures at 120, 130, 140, 150 ºC, using heating mantle (Lab Hosp. Corp., ELCON)
and the molten polymer was cooled at room temperature and then milled using
hammer mill(Lab Hosp).The obtained granules of different processing temperature
were then compared for their appearance and discoloration .
Table 1: ND FORMULATION
Ingredient |
Applications |
Quantity per tablet(mg) |
Dap |
Drug |
100 |
Lactose
monohydrate |
Diluent |
33 |
Microcrystalline
Cellulose |
Diluent |
33 |
Crospovidone |
Disintegrant |
8 |
Magnesium Stearate |
Lubricant |
1 |
Total |
|
175 |
5.
Preparation of Non HME (ND) Formulation[As
control sample]:
Dap (as such), lactose monohydrate,
microcrystalline cellulose and crospovidone as in table
1 are (sifted through #40 sieve) mixed well for 5 min. Prepared dry mix
lubricated by magnesium stearate (sifted through # 60
sieve) for 3 min. Lubricated granules were evaluated for flow properties and
compressed into tablets.
6.
Effect of type and concentration of
plasticizer on solubility and dissolution:
Dap, polymer and plasticizer as in table 2
were mixed well and taken in porcelain dish. This dry mix was subjected to melt
at 175°C using heating mantle (Lab
Hosp. Corp., ELCON) with mixing to get clear molten mass. Curing of molten mass was done by keeping it
at room temperature for 12 hrs.
a.
Size Reduction of HME Flakes:
Solid dispersion prepared by
HME was then passed through 3mm screen of hammer mill, milled granules were
sifted through #40 sieve. Granules retained on #40 sieve
then passed through 1mm screen of hammer mill, milled granules were sifted
through #40 sieve. Obtained granules were mixed well for 5min.
Table 2: HME FORMULATION
|
Applications |
D1 |
D2 |
D3 |
D4 |
D5 |
D6 |
D7 |
D8 |
D9 |
Dry
mix for HME |
|
mg/tab |
mg/tab |
mg/tab |
mg/tab |
mg/tab |
mg/tab |
mg/tab |
mg/tab |
mg/tab |
Dap |
Drug |
100 |
100 |
100 |
100 |
100 |
100 |
100 |
100 |
100 |
Kollidon VA64 |
Thermal binder |
100 |
100 |
100 |
100 |
100 |
100 |
100 |
100 |
100 |
PEG 4000 |
Plasticizer |
10* |
- |
- |
20** |
30# |
- |
- |
- |
- |
Cremophor EL |
Plasticizer |
- |
10* |
- |
- |
- |
20** |
30# |
- |
- |
Montane 20 PHA |
Plasticizer |
- |
- |
10* |
- |
- |
- |
- |
20** |
30# |
HME
Granules |
|
210 |
210 |
210 |
220 |
230 |
220 |
230 |
220 |
230 |
Lubricants |
|
|
|
|
|
|
|
|
|
|
Colloidal Silicon Dioxide |
Lubricant |
1.3 |
1.3 |
1.3 |
1.3 |
1.3 |
1.3 |
1.3 |
1.3 |
1.3 |
Sodium Stearyl Fumarate |
Lubricant |
2.7 |
2.7 |
2.7 |
2.7 |
2.7 |
2.7 |
2.7 |
2.7 |
2.7 |
Total |
|
214 |
214 |
214 |
224 |
234 |
224 |
234 |
224 |
234 |
*10% w/w of polymer (Kollidon VA 64)
**20% w/w of polymer (Kollidon VA 64)
#30% w/w of polymer (Kollidon VA 64)
b.
Lubrication of HME Granules:
HME granules were then
lubricated by sodium stearyl fumarate
and colloidal silicon dioxide (sifted through #60 sieve)
for 5 min. Lubricated granules were
evaluated for flow properties and compressed into tablets. Compression
parameters were recorded.
c.
Characterization of HME Dry Mix ,HME
Granules And NHME Dry Mix:
i.
DSC:
The drug, HME and NHME were
subjected to DSC study using (Mettler TA 4000) DSC
apparatus. First 5-10 mg of sample was weighed into aluminum crucible. These
powders/granules were analyzed by heating at scanning rate of 100C /
minute over a temperature range 50 to 2000 C with nitrogen flow of 50mL/min.
ii. XRD:
The drug, HME complex and NHME formulated
powder were subjected to XRD (using P.W. 1729, X-Ray Generator, Philips, Nether
land). To study XRD pattern, the sample was placed into aluminum holder and the
instrument was operated between initial and final 2θ angle of 5-500 respectively
in an increment of 0.402θ.
iii. IR:
The drug,
HME complex and NHME formulated powder were subjected to FTIR (8400s
spectrophotometer Shimadzu) studies to check the characteristic sharp peaks of
drug and its functional groups. The KBr disk method
was used for preparation of sample.
Prepared tablets (table 2) of
formulation F1 –F9 were subjected to solubility and dissolution study.
7.
In Vitro Permeability of HME and NHME
Formulation:
The prepared tablets were
subjected to In vitro permeability test using dialysis membrane LA401.
8.
Stability Studies:13
Stability studies of tablets
were performed as per International Conference on Harmonisation
(ICH) guidelines. The tablets from the optimized batch were subjected for
stability study at 40ºC/75% RH for 3 months.
RESULT AND DISCUSSION:
1.
Characterisation
of Dap:
A.
Description:
B.
It is
a white, odorless crystalline powder. Hence confirms the description as per the
certificate of analysis (COA).
C. Saturation
Solubility:
As per literature the solutbility of Dap in water is less than 380µg/mL. Experimentally it was found to be 3.703952381µg/mL.
D.
Melting point:
Melting point by capillary
method and instrumental method observed was 170⁰C and 175⁰C respectively. (as per the literature
175ºC)
E.
XRD:
Sharp peaks were observed from
5 to 30º of 2θ scale, which reveals the crystalline nature of drug.
F.
IR:
IR spectra reveal
characteristic functional groups same as reference standard.
G.
DSC:
DSC studies show the peak
value at 175⁰C corresponds to standard melting point (175.5ºC).
All the characteristic test of
pure drug confirms the purity of Dap.
2.
Preparation of Standard Curve:
Dap is soluble in dilute HCl 2mL, so this
medium was used for preparation of standard curve. λ
max, correlation coefficient R and calibration curve equation are as given
below.
Using absorbance and concentration data Beer lamberts plot was prepared
which is shown in figure 1 and table 3. Calibration curve equation has shown
linear relationship and high degree of correlation in the range of 1-10 μg/mL at 288nm. This curve
was utilized in Dap estimation as and when required
Figure 1: CALIBRATION CURVE FOR DAP
Table 3: CALIBRATION CURVE
FOR DAP (n=3)
Concentration (µg/mL) |
Average Absorbance |
1 |
0.009±0.001 |
2 |
0.0416±0.001 |
3 |
0.0845±0.002 |
4 |
0.1331±0.001 |
5 |
0.178±0.005 |
6 |
0.2211±0.002 |
7 |
0.2612±0.003 |
8 |
0.2981±0.001 |
9 |
0.3422±0.002 |
10 |
0.3858±0.001 |
3.
Determination of Drug :Polymer Ratio
Initially all the prepared
films were transparent as in table 4. Appearance of these films even after
storage at room temperature for 24hrs remained transparent except film of pure
drug which on storage shows the recrystallization of
drug. In all other ratios of drug: polymer (1:1 to 1:5). Dap remain in solubilised state throughout the storage period as in
figure 2. So 1:1 ratio was selected for further study as Dap
remains in solubilised state in this ratio.
Table
4: OPTIMISATION OF DRUG: POLYMER RATIO
|
Sample |
Solvent |
Ratio |
Solubility |
Appearence |
Appearance after 24 hrs |
A |
Drug |
Ethanol |
- |
Clear solution |
Clear, transparent |
White clusters
were seen |
B |
Polymer |
Ethanol |
- |
Clear solution |
Clear, transparent |
Clear, transparent |
C |
Drug: Polymer(1:1) |
Ethanol |
1:1 |
Clear solution |
Clear, transparent |
Clear, transparent |
D |
Drug: Polymer(1:2) |
Ethanol |
1:2 |
Clear solution |
Clear, transparent |
Clear, transparent |
E |
Drug: Polymer(1:3) |
Ethanol |
1:3 |
Clear solution |
Clear, transparent |
Clear, transparent |
F |
Drug:Polymer(1:4) |
Ethanol |
1:4 |
Clear solution |
Clear, transparent |
Clear, transparent |
G |
Drug:Polymer(1:5) |
Ethanol |
1:5 |
Clear solution |
Clear, transparent |
Clear, transparent |
Figure
2: Appearance of films after 24 hrs (at room temperature and in desiccators),
a: pure drug, b: polymer, c: drug: polymer (1:1), d: drug: polymer (1:2), e:
drug: polymer (1:3), f: drug: polymer (1:4), g: drug: polymer (1:5)
Figure 3: TEMPERATURE RANGE FOR EXTRUSION
OF PURE POLYMERS
4.
Effect of Temperature on Decomposition of
Polymer
Extrudates of Kollidon VA64
look clear and glassy, with increasing temperature the colour
turns yellowish and brownish. The actual discolouration
of polymer was observed above 120⁰ C
processing temperature. Above 200⁰C melting
temperature extrusion becomes difficult.
5.
Preparation of Non HME Formulation
Lubricated granules
characterization and compression parameters are as given below in table 5.
6.
Effect of type and concentration of
plasticizer on solubility and dissolution:
Glass transition temperature (Tg) (figure 3) of Kollidon VA64 is 101⁰C, which
may be reduced after addition of plastisizers. As a
general rule, melt extrusion process should be run at temperature 20-40⁰C above the Tg. Temperature range for melt extursion of
pure polymer is 155-200⁰C where as for polymer plastisizer
combination it is 120-200⁰C
Table 5: EVALUATION OF LUBRICATED
GRANULES AND TABLETS-ND (n=3)
Parameters for
granules |
Observations |
Bulk Density(g/mL) |
0.55±0.022 |
Tapped density(g/mL) |
0.64±0.012 |
Hausner’s Ratio |
1.16±0.01 |
Carr’s Index (%) |
14.06±0.07 |
Angle of repose (⁰ ) |
25±0.034 |
Parameters for tablets |
Observations |
Machine |
Lab Hosp |
Punch |
8mm,Tablet shape |
Weight of tablet(mg) |
175±0.011 |
Hardness(kg) |
10±0.061 |
Disintegration Time(mins) |
8±0.51 |
Friability (%) |
0.3±0.801 |
In melt extrusion process drug can be
either dissolved or dispersed in an amorphous or crystalline state. To obtain thermodynamically
stable formulation drug must get completely dissolved below its saturation
solubility in the polymer which is known as solid solution .When the main
objective of melt extrusion technology is enhancement of solubility, the
processing temperature should be equivalent or slightly higher than melting
point of drug to get solid solution system. Melting point of Dap is
approximately 175⁰C (by DSC method), so the 180⁰C temperature was selected for melt extrusion processing to get
solid solution.
a.
Size Reduction and Lubrication of Granules
As compared to
NHME granules, dense granules were obtained by HME process. Increased bulk and
tapped density values confirmed the presence of dense granules. Hausner’s ratio, carr’s
index and angle of repose values reveals the good flow characteristics of
granules (table 6). Disintegration time of tablets prepared by HME technology
was three times higher than those prepared by NHME technology (table 6).
Disintegration pattern was bursting and erosion in tablets prepared by NHME and
HME technology respectively.
b.
Characterization of Drug, HME Granules And
NHME Dry Mix
Absence of sharp peak was observed in DSC
of HME granules as compared to DSC of pure drug. This indicates the presence of
amorphous drug in molten carrier, but in case of NHME the sharp peak was
observed indicating the crystalline nature of drug. DSC thermograms of Dap in NHME and Dap HME granules represented
in the figure 4I. The DSC thermograms of pure
Dap shows sharp endotherm at 1750C
attributed to the melting of Dap. This sharp melting endotherm
indicates the crystalline nature of drug. The DSC thermogram of NHME shows melting at 159 and 1810C
of the drug and polymer respectively. The DSC thermogram
of HME PEG, HME Chremophor and HME Montane 20PHA shows absence of characteristic melting endotherm of Dap indicating the perfect miscibility of drug
and polymer in the solid dispersion. As single Tg is characteristic of the thermoplastic system, the
DSC thermogram of solid dispersion shows complete amorphization of drug.
Table
6: EVALUATION OF LUBRICATED GRANULES AND TABLETS-HME (n=3)
Parameters
for granules |
Observations |
||
|
D1 |
D2 |
D3 |
Bulk
Density(g/mL) |
0.52±0.15 |
0.512±0.11 |
0.501±0.033 |
Tapped
density(g/mL) |
0.67±0.04 |
0.64±0.001 |
0.63±0.019 |
Hausner’s Ratio |
1.28±0.11 |
1.25±0.04 |
1.26±0.064 |
Carr’s
Index (%) |
22.38±0.021 |
20±0.061 |
20.48±0.27 |
Angle
of repose(⁰) |
27±0.01 |
26±0.023 |
28±0.022 |
Parameters
for tablets |
D1 |
D2 |
D3 |
Machine |
Lab. Hosp. |
||
Punch |
9mm,Tablet shape |
||
Weight
of tablet(mg) |
214mg |
224mg |
234 mg |
Hardness(kg) |
10 kg±0.06 |
10 kg±0.09 |
10 kg±0.01 |
Disintegration
Time(min) |
24mins±0.01 |
25mins±0.036 |
23mins±0.088 |
Friability(%) |
0.3%±0.01 |
0.31%±0.08 |
0.36%±0.037 |
Figure 4I: DSC OF A) PURE DRUG B) NHME C) HME PEG D) HME
CHREMOPHOR E) HME MONTANE 20 PHA
Figure
4II: XRD OF A) DRUG B) NHME C) HME PEG D) HME CHREMOPHOR E) HME MONTANE 20 PHA
Figure 4III: FOURIER TRANSFORM INFRARED OF A) PURE DRUG B) NHME C)
HME PEG D) HME CHREMOPHOR E) HME MONTANE PHA
7. The XRD pattern of pure drug, NHME, HME
PEG, HME Chremophor and HME Montane
PHA were recorded between 0-50 2θ scale
and represented in the following figure 4II. The XRD pattern of pure drug shows
several diffraction peaks indicating the crystalline nature of the drug. Peaks
for crystallinity were observed in pure drug (Figure No. 4II a). The XRD pattern of NHME
showed the presence of peaks with a significant decrease in intensity or
absence of some major dap crystalline peaks (Figure No. 4II c). Generally this
partial loss of crystallinity may be observed due to
physical presence of amorphous excipients and their
higher concentration. The drug was still in the crystalline state in this
system. The XRD patterns of HME PEG, HME Sorbiton and
HME montane 20 PHA showed complete absence of peaks
of crystallinity as observed in pure Dap indicated
complete amorphization of Dap in the melt. The
presence of hump in all the samples indicates the amorphous nature of drug in
the HME granules (Figure 4II c, d, e).
8. From the FTIR study Figure 4III it is clear
that there is no interaction between drug PEG, drug chremophor, drug montane 20 PHA.
All the peaks were responsible for active functional groups which were even
present in HME granules of different types. In NHME similar peaks were observed
as that of pure drug indicating no complex formation between drug and polymer.
9.
Dissolution and saturation solubility
Saturation solubility data
(table 7) indicates that the hot melt process improved the solubility of Dap by
4 times, 25 times and 74 times of its original solubility by using PEG 4000, Cremophor
EL and Montane 20 PHA respectively. As compared to
encouraging results of saturation solubility, dissolution data didn’t showed
any noticeable discrimination in different plasticizers. So, it was decided to
do the further study by using 10% w/w concentrations of plasticizers. Increased
concentration of plasticizers didn’t show any noticeable improvement in
saturation solubility.
From the results of saturation solubility
10% was further optimized for dissolution studies. The average dissolution is
as given below in figure 5. The disintegration time of tablets prepared by HME
process was thrice more than DT of NHME and marketed formulations. Increased
concentration of plasticizer did not show any improvement in dissolution rate.
So, as a discriminative method to determine the dissolution enhancement by HME
technique the in vitro permeability of formulations containing 10% plasticizer
(using dialysis membrane in disso apparatus) was performed.
Figure 5: Dissolution studies of various
formulations with for 10% peg 4000 =
38, 10% chremophor el = 36, 10% montane
20pha = 46
10.
In vitro permeability of HME and NHME
formulation
In vitro permeability study
shows (Figure 6) that the Dap HME tablets prepared by 10% PEG4000 have highest
permeability as compared to other Dap HME tablets. NHME tablets shows lowest in
vitro permeability compared to all Dap HME formulations, even though have
higher dissolution rate.
Increase in, in vitro
solubility and permeability may increase the in vivo solubility and
permeability which leads to reduction in some fold of Dap dose and cost of
dosage form.
Figure 6: Permeabiltiy
Studies
Stability Study
Stability study (table 8) was
carried out to determine the physical stability of the formulation carried out
as per ICH guidelines at 40±20 C and 75% ±50C RH for 1, 2
and 3 months. Various tests such as the drug content, moisture content and
dissolution were carried out at the end
of 1, 2 and 3 months and compared with the day 0 results.
Table
8: STABILITY STUDIES (n=3)
Formulation |
D1 |
D2 |
D3 |
|||||||||
Storage Condition |
400±20C/75%±5%RH |
|||||||||||
Storage Period |
Initial |
1M |
2M |
3M |
Initial |
1M |
2M |
3M |
Initial |
1M |
2M |
3M |
Physical Appearance |
Good |
Good |
Good |
Good |
Good |
Good |
Good |
Good |
Good |
Good |
Good |
Good |
Moisture Content (%) |
1.3± 0.12 |
1.3± 0.75 |
1.4± 0.34 |
1.4± 0.04 |
1.5± 0.02 |
2.0± 0.75 |
2.2± 0.05 |
2.8± 0.03 |
2.8± 0.31 |
2.9± 0.51 |
3.6± 0.024 |
3.7± 0.24 |
Drug Content (%) |
99.2± 0.06 |
99.11± 0.01 |
98.97± 0.07 |
98.7± 0.017 |
99.00± 0.08 |
98.88± 0.28 |
98.12± 0.33 |
97.11± 0.85 |
98.2± 0.85 |
98.01± 0.50 |
97.99± 0.32 |
97.12± 0.64 |
Dissolution (%) at 150min |
95.02± 0.22 |
94.11± 0.89 |
93.93± 0.36 |
93.2± 0.09 |
93.57± 0.21 |
93.10± 0.01 |
92.90± 0.85 |
91.81± 0.36 |
94.17± 0.28 |
93.88± 0.01 |
93.2± 0.85 |
92.01± 0.92 |
CONCLUSION:
Solubility of Dap can be increased by HME
technology which is one of the method of solid
dispersion. The XRD pattern shows amorphous nature of Dap in HME granules. The
DSC thermogram of HME granules shows absence of
characteristic melting endotherm of Dap indicating
the perfect miscibility of drug and polymer in the HME granules. Dissolution
rate of Dap HME tablets is not similar to that of NHME and marketed
formulations, but the saturation solubility and in vitro permeability of Dap
HME formulations is higher than NHME and marketed formulations. In all HME
formulations HME with PEG4000 shows better enhancement in, in vitro
permeability and saturation solubility. All optimized HME formulations shows
good stability over the period of 3 month at 400±20C/75%±5%RH.
ACKNOWLEDGEMENT:
Authors are thankful to Emcure
Pharma Ltd, BASF pharma
ltd, Modern College of Pharmacy (For Ladies) Moshi
and University of Pune for their support.
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Received on 31.10.2013 Accepted on 01.12.2013
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Asian J. Res.
Pharm. Sci. 2013; Vol. 3: Issue 4, Pg 206-214