CRITICAL ROLES PLAY OF MAGNESIUM STEARATE IN FORMULATION DEVELOPMENT OF A HIGHLY SOLUBLE DRUG METFORMIN HYDROCHLORIDE
HTML Full TextCRITICAL ROLES PLAY OF MAGNESIUM STEARATE IN FORMULATION DEVELOPMENT OF A HIGHLY SOLUBLE DRUG METFORMIN HYDROCHLORIDE
Meenakshi Shadangi, Saurabh Seth* and Deepak Senapati
Ajanta Pharma Limited, Kandivali (W), Mumbai, Maharashtra, India
ABSTRACT
This article is giving emphasis on the decisive role of particle size of highly hydrophobic lubricant i.e. Magnesium Stearate, its concentration and lubrication time to establish the desired quality attributes of formulation containing highly soluble model drug Metformin Hydrochloride. Magnesium Stearate from two sources with different Particle size distribution (PSD) range was selected. It was observed that the Magnesium Stearate with a designed PSD is controlling the drug release profile of Metformin hydrochloride Tablets, which can replace the use of excess quantity of Magnesium Stearate or addition of a rate controlling polymer like hydroxy propyl methyl cellulose in the formulation design.
Keywords:Magnesium Stearate,
Metformin Hydrochloride, Particle Size, |
Surface Area
INTRODUCTION:Among the tablet excipients, lubricants are extremely important for improving the quality and manufacturing productivity of the tablets. Lubricants reduce the friction between the tablet edge and the die wall during compression and facilitate ejection by forming a film of low shear strength between the die wall and tableting mass 1, 2.
Magnesium Stearate exists as “Plate-like” crystals (or lamellae) stacked together like a deck of cards. As the blending process proceeds, plates continue to shear off and coat adjacent particles of granules, drug or other excipients. The higher the concentration of Magnesium Stearate used or the longer this blending continues, the more complete this coating of the adjacent particles will become.
It has low friction coefficient and high covering potential. The lubricant efficiency and extent of surface coverage depend on the mixing time of the tablet mass with Magnesium Stearate because of its laminar structure 3.
Introduction of the high-speed tableting machine requires the use of higher concentrations of Magnesium Stearate, but increasing concentration of Magnesium Stearate can adversely affect the flow properties of the tableting mass and the quality properties of tablets 4, 5, 6.
Therefore, the concentration of the lubricant in the formulations and the lubrication time should be balanced in terms of the adverse effects of the used lubricant. Generally, lubricants are added to the premixed powder mixture as a final step and mixed for only a few minutes. But even small changes in mixing time and lubricant amount can significantly affect the product performance and quality properties.
As a result of over-lubrication, the mechanical strength of the tablets can decrease and the dissolution of the drug may worsen. Therefore, experiments should be performed to define lubricant use level and optimize the mixing process.
The particle size and specific surface area of Magnesium Stearate may be the key factors influencing its lubrication efficiency. In practice, the particle size, instead of the surface area, is much more often used as a measure of the lubricant characteristics. It is mainly due to the fact that particle size measurement of a powder material is faster, easier, and less controversial 7.
Metformin is the only currently available oral antidiabetic or hypoglycaemic agent which acts predominantly by inhibiting hepatic glucose release with an absolute oral bioavailability of 40% to 60% 8. Gastrointestinal absorption occurs mainly in the upper intestine with peak plasma concentrations (Cmax) reaching after 2 to 3 h 9. Metformin HCl is a BCS class III drug (Highly solubility and Low permeabiality).
The present study was designed with an objective of further evaluating the influence of Lubrication process on Tablet performance with three independent variables: Level of Lubricant, Lubricant Particle size and Lubrication Time on various selected responses. The measured responses from tablets were the Carr’s Index, Hausner ratio, percentage of friability, hardness, disintegration, and percent drug dissolved in 10, 15, 30 and 45 min.
Further, it was aimed at optimizing independent variables to achieve similar dissolution profile of Reference product.
MATERIAL AND METHODS:
Materials: Metformin HCl was manufactured in Granules India Ltd, Hyderabad, (India). Povidone K30 and Povidone K90 were procured from ISP, USA. Pregelatinized starch was procured from Roqutte, (USA). Magnesium Stearate was procured from Nitika Chemicals, Nagpur, (India) and Mallinckrodt baker, USA. Glucophage 1000 mg tablets were purchased commercially from market for comparative study. All other reagents and chemicals were of analytical grade and used as received.
Methods:
Granulation: 2.79 kg Metformin HCl was mixed with 0.12 kg of Povidone K30 in an octagonal blender (Shan engineers) for 5 minutes. Binder solution was prepared by dissolving 0.09 kg Povidone K90 and 0.12 kg Povidone K30 in 0.80 kg of Purified hot water at 60-65oC. Metformin granules was made in Fluidized bed Processor (Glatt FBE-5) having 5L capacity. Granulation was done by spraying the binder solution using top spray method. The process parameters were kept same for all the experiments as given in Table 1.
TABLE 1: SET PROCESS PARAMETERS FOR TOP SPRAY GRANULATION OF METFORMIN HCL GRANULES
Process Parameters | Set value |
Inlet temperature (oC) | 70-90 |
Exhaust temperature (oC) | 45-55 |
Bed temperature (oC) | 30-45 |
Peristaltic pump RPM | 25 |
Spray Rate (gm/min) | 30-35 |
Atomization (MPa) | 0.25-0.35 |
Air flow (m/s) | 3.5-4.5 |
Granules were dried in the FBP upto LOD 0.8-1.5%w/w and sifted through 16# and sieve tops were milled through multimill using 1.5 mm screen. Granules were lubricated in Octagonal blender of 10 L capacity (Shan Engineers).
Determination of Flow Properties of Lubricated Granules: The bulk density of lubricated granules was determined by pouring 100.0 gm of granules into 250.0 mL graduated measuring cylinder through a funnel. The tapped density was measured by USP method 1 using tapped density apparatus (Electrolab, India). Carr’s index (CI) was estimated from the bulk and tap volumes (Vbulk and Vtap) according to Eq. 1.
Vbulk – Vtap
CI% = ------------------- X 100 …....................... (Eq.1)
Vbulk
Hausner index (HI) was calculated from the BD and TD values (Eq. 2).
HI = TD/ BD ....................................................(Eq.2)
Preparation of Tablets: The lubricated granules were compressed into 1000 mg oval shaped Tablet using Compression machine (Rimeck, 12 stations, Minipress IISF).
Evaluation of Tablet properties:
Hardness Test: Twenty tablets taken randomly from each batch were tested for hardness using hardness tester (Pharmatest, Incorp). The average hardness (Kp) and standard error were calculated for each batch.
Friability Test: Twenty tablets were taken randomly and weighed accurately and placed in a friabilator (Electrolab, India). After 100 rotations (25 rotations per minute, for 4 min), the tablets were removed and re-weighed accurately. The loss in mass was determined 10.
Disintegration Test: One tablet was placed in each tube of the basket rack assembly and a disc was added on each tube. The rack was immersed in distilled water at 37±2ºC and the apparatus (Electrolab, India) was operated at a frequency rate between 29-32 cycles per minute. The time (min) to disintegrate and fall of the tablets through the screen was recorded 10.
Dissolution Test: Dissolution studies on the tablets of Metformin HCl were conducted in USP Apparatus 1 (basket method) (Electrolab TDT-08L, India) with three replicates, according to the USP monograph 11. The dissolution medium was 1000 mL of pH 6.8 phosphate buffer at 37±0.5oC. The basket rotation speed was kept at 100 rpm. In all experiments, 5 mL of dissolution sample was withdrawn at 5, 10, 15, 30, and 45 min and replaced with an equal volume of the fresh medium at 37±0.5oC to maintain a constant total volume. Samples were assayed by UV spectrophotometry at the wavelength of maximum absorbance at about 233 nm (Shimadzu UV-2450, Japan). Cumulative percentages of the drug dissolved from the tablets were calculated.
In order to compare the drug release profile of formulations with the reference product, similarity factor (f2 value) has been calculated using the following formula-
f2 = 50 • log {[1 + (1/n) Σt=1n (Rt - Tt) 2]-0.5 • 100}
The similarity factor is a logarithmic reciprocal square root transformation of the sum of squared error and is a measurement of the similarity in the percent (%) of dissolution between the two curves. Two dissolution profiles are considered similar when the f2 value is ≥ 50 12.
Experimental Design: The lubricant concentration in powder mixtures, Particle size distribution of lubricant and the length of lubricant mix time were the independent factors. The dependent factors were the measured responses from powder mixtures before tableting, that is, Compressibility index (CI) and Hausner ratio (HR). The measured responses from tablets were percent friability (FRI), Hardness (HD), Disintegration time (DT) and percent drug dissolved in 10, 15, 30 and 45 min. The particle size and surface area data for Magnesium Stearate are given in Table 2. A two-factor, three-level full factorial design (32) was formed for Magnesium Stearate (A and B), to clarify the effects of independent factors on measured responses. Total 18 experiments were designed based on the independent factors. The codes for studied batches, range of the independent factors and measured responses for dependent variables are shown in Table 3.
TABLE 2: PARTICLE SIZE AND SURFACE AREA OF MAGNESIUM STEARATE
Code of Magnesium Stearate |
Particle size Distribution (PSD) | Specific Surface area | |
A(Nitika) | D(50)= | 40.8 microns | 4.15 m2/gm |
D(90)= | 71.3 microns | ||
B(Mallinckrodt Baker) | D(50)= | 12.7 microns | 6.4 m2/gm |
D(90)= | 23 microns |
RESULT & DISCUSSION:
Lubricated Blend Flow Characteristics: Although it was physically observed that on increasing Magnesium Stearate concentration, the flow of the lubricated blend was slightly decreased, through hopper to turret, yet no significant difference was observed on CI and HR.
Tablet Properties: As shown in Table 3, on increasing the concentration of Magnesium Stearate (A) from 0.75% to 1.25% w/w along with blending time disintegration time was increased slightly. The friability of tablets was slightly increased on increasing concentration of Magnesium Stearate. Dissolution profile of tablets was improved in order to get the target dissolution profile of reference standard, but still desired profile was not achieved. The similarity factor (f2 value) was observed below 50. Further increase in Magnesium Stearate concentration has affected the physical properties of tablets and capping was also observed.
It is also not wise to use higher concentration of Magnesium Stearate in the formulation because with large batch size improper mixing of Magnesium Stearate may cause variation in release pattern.
In next set of trials (F10-F18), with Magnesium Stearate (B) having reduced particle size and larger surface area, we observed that increase in the concentration and blending time have significant effect on tablets physicochemical properties due to reduced particle size of Magnesium Stearate. In trials F1 and F10, at the same level of concentration of Magnesium Stearate (A and B) and blending time, the disintegration time of the tablets were increased from about 9 minutes to about 14 minutes. In trials F17 and F18, tablets were showing capping problem when hardness was tried to keep in between 12-16
Kp. Therefore, tablets were compressed at rather lower hardness. Friability was also observed somewhat higher than formulations F1-F9.
Formulation having 0.75% w/w Magnesium Stearate (B) and 15 min blending time showing Similarity factor 92.2. With higher concentration of Magnesium Stearate 1.0% w/w and 1.25% w/w with blending time 10 and 15 minutes, respectively nearly same result was observed. With 1.25% w/w concentration, on increasing blending time the drug release from the tablet was incomplete in desired time frame as well as capping problem was also observed due to over coating of hydrophobic layer on granules.
As far as tablet hardness and capping problem is concern in Metformin HCl tablets, it was observed that, apart from Magnesium Stearate, moisture content in lubricated granules is also plays a vital role. If moisture level was kept below 0.8% w/w, capping was observed during compression. On the other hand, if moisture level was exceeding from 1.5% w/w, tablets were unable to achieve desired hardness. To avoid the effect of moisture level on tablets, in all the trials moisture level of lubricated blend was kept in between 0.8-1.5% w/w.
TABLE 3: COMPOSITIONS OF THE STUDIED FORMULATIONS AND THE MEASURED RESPONSES
Code | Independent factors | Dependent factors | |||||||||||
Particle size | Lubrica-tion conc. | Mixing time | CI | HR | FRI | HD | DT (Min.Sec) | Dissolution | |||||
10 min | 15 min | 30 min | 45 min | F2 value | |||||||||
F1 | A | 0.75% | 5 | 13.8±1.2 | 1.12±0.21 | 0.242±0.025 | 14.3±1.5 | 8.52±0.24 | 82.8±2.5 | 90.3±1.8 | 99.1±1.8 | 102.4±0.75 | 25.3±3.5 |
F2 | A | 0.75% | 10 | 14.2±1.7 | 1.16±0.34 | 0.257±0.018 | 12.8±1.8 | 8.47±0.33 | 81.5±3.1 | 91.2±1.5 | 97.2±1.0 | 100.8±0.8 | 25.7±2.8 |
F3 | A | 0.75% | 15 | 13.3±1.1 | 1.14±0.15 | 0.254±0.023 | 13.6±2.1 | 9.12±0.28 | 81.2±3.2 | 90.7±2.4 | 96.7±2.1 | 101.3±1.2 | 25.9±4.6 |
F4 | A | 1.00% | 5 | 15.1±0.8 | 1.23±0.18 | 0.219±0.037 | 14.1±1.9 | 9.54±1.06 | 76.5±3.5 | 88.4±2.7 | 94.5±1.6 | 99.4±0.58 | 28±3.4 |
F5 | A | 1.00% | 10 | 14.6±1.6 | 1.19±0.27 | 0.388±0.041 | 12.6±1.5 | 8.46±0.47 | 74.8±4.1 | 85.5±2.8 | 93.9±1.7 | 100.5±1.1 | 29.3±3.3 |
F6 | A | 1.00% | 15 | 15.4±1.2 | 1.24±0.21 | 0.345±0.028 | 12.3±1.4 | 10.15±0.25 | 73.1±3.4 | 82.5±2.3 | 92.7±1.9 | 98.8±0.9 | 30.3±4.2 |
F7 | A | 1.25% | 5 | 16.0±1.4 | 1.21±0.28 | 0.347±0.038 | 14.3±1.3 | 9.30±0.49 | 67.5±2.7 | 80.1±1.8 | 91.4±1.3 | 99.9±0.7 | 33.6±2.9 |
F8 | A | 1.25% | 10 | 16.1±1.2 | 1.11±0.19 | 0.339±0.042 | 14.7±1.6 | 10.58±1.02 | 67.1±4.6 | 78.5±2.7 | 90.4±2.0 | 102.1±1.8 | 34.3±3.3 |
F9 | A | 1.25% | 15 | 16.8±1.5 | 1.13±0.22 | 0.319±0.026 | 13.2±2.1 | 11.12±0.36 | 64.5±5.6 | 77.8±3.2 | 89.8±2.4 | 99.4±1.5 | 35.8±2.7 |
F10 | B | 0.75% | 5 | 14.5±1.2 | 1.26±0.31 | 0.473±0.035 | 13.8±1.1 | 13.39±0.46 | 58.8±5.2 | 67.9±3.6 | 90.1±2.4 | 98.9±2.2 | 42.5±3.8 |
F11 | B | 0.75% | 10 | 16.8±1.1 | 1.22±0.15 | 0.436±0.027 | 13.5±1.5 | 13.15±0.54 | 46.7±4.7 | 59.5±3.8 | 87.4±2.6 | 97.2±1.1 | 57.9±2.5 |
F12 | B | 0.75% | 15 | 15.9±1.2 | 1.13±0.11 | 0.318±0.031 | 13.8±1.2 | 13.54±0.55 | 38.0±3.7 | 51.9±2.2 | 81.6±1.3 | 95.8±0.7 | 92.2±2.2 |
F13 | B | 1.00% | 5 | 16.8±1.5 | 1.20±0.33 | 0.331±0.021 | 14.1±1.7 | 13.48±0.38 | 48.2±4.2 | 66.4±2.9 | 91.7±1.8 | 100.5±0.8 | 55.0±3.7 |
F14 | B | 1.00% | 10 | 16.5±0.8 | 1.31±0.31 | 0.419±0.019 | 13.2±1.4 | 14.56±1.24 | 38.6±5.1 | 51.6±3.2 | 80.5±2.6 | 94.4±1.8 | 90.4±1.8 |
F15 | B | 1.00% | 15 | 17.6±0.6 | 1.25±0.24 | 0.404±0.042 | 13.6±1.1 | 14.38±1.07 | 35.6±4.2 | 48.3±2.4 | 77.2±2.1 | 96.5±2.2 | 78.4±2.8 |
F16 | B | 1.25% | 5 | 19.4±1.1 | 1.30±0.23 | 0.458±0.033 | 11.4±1.8 | 16.45±0.58 | 39.8±4.8 | 52.4±3.6 | 83.1±2.6 | 97.4±2.7 | 84.0±1.1 |
F17 | B | 1.25% | 10 | 20.1±0.8 | 1.37±0.21 | 0.563±0.047 | 10.7±2.2 | 18.11±1.22 | 33.1±3.7 | 44.9±2.5 | 70.6±1.8 | 85.8±1.5 | 53.8±2.8 |
F18 | B | 1.25% | 15 | 19.7±1.3 | 1.29±0.15 | 0.584±0.040 | 10.5±1.3 | 18.5±1.04 | 29.8±5.6 | 41.4±3.7 | 68.0±2.5 | 84.7±2.1 | 48.4±1.6 |
n=3, Mean±SD
FIG. 1: DISSOLUTION PROFILE OF ALL THE FORMULATIONS
FIG. 2: SIMILARITY FACTOR (f2 VALUE) OF FORMULATIONS
CONCLUSION: This study concluded that the change in particle size hence surface area of Magnesium Stearate, along with concentration and lubrication time, can affect the properties of a blend or tablets significantly, such as disintegration time, hardness and most importantly dissolution. The tablets, containing Magnesium Stearate of larger particle size, have shown the highest percentage of drug release at initial time points as a consequence of poor hydrophobic coating on granules of highly soluble drug. However, tablets contain Magnesium Stearate with smaller particle size and larger surface area had shown a slower drug release profile.
The study investigated that by selecting appropriate particle size of Magnesium Stearate along with some other factors like lubrication concentration and blending time, we can achieve the desired release profile and a very high quality, cost effective formulation.
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Article Information
43
1188-1193
489KB
3204
English
IJPSR
Meenakshi Shadangi, Saurabh Seth* and Deepak Senapati
Ajanta Pharma Limited, Kandivali (W), Mumbai, Maharashtra, India
10 January, 2012
16 March, 2012
28 March, 2012
http://dx.doi.org/10.13040/IJPSR.0975-8232.3(4).1188-93
01 April, 2012