preparation & evaluation of tablets from ma &...
TRANSCRIPT
Preparation & Evaluation of Tablets
from MA & Optimized
Agglomerates.
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 303
11. Preparation and evaluation of Tablet dosage form by direct compression
method:
Compactibility is the process of volume reduction and bond formation in a powder bed
during compression, which produces compacts of a certain mechanical strength. When
pressure is applied to a powder bed, particle rearrangement occurs first, followed by
particle fragmentation and deformation (plastic and elastic deformation), and bond
formation on the contact surfaces (1). Plastic deformation is an irreversible process of
particle shape changing that contributes to stronger tablets, while elastic deformation is
reversible and leads to elastic recovery of compacts in the decompression phase and the
breakage of some previously formed bonds, which results in lower tablet strength and
capping problems. In the case of plastically flowing material, the particle shape changes
during compression, but the surface area remains nearly unchanged.
On the other hand, primary particles of materials that fragment (break) into smaller parts
during compression, lead to an increased surface area and increased number of contact
points suitable for bond formation. In both cases plastic deformation occurs at later stages
of compression and adequate tablet strength can be obtained. Typical examples of
materials with mainly plastic flow include microcrystalline cellulose (MCC), typical
materials that mainly fragment include dicalcium phosphate dihydrate, crystal lactose,
etc. (2-3).
The main bonding mechanisms involved in compact formation are:
1. Solid bridges, which represent the strongest bonds between particles.
2. Intermolecular or long distance forces (van der Waals forces, electrostatic forces,
hydrogen bonding), representing weaker attraction forces.
3. Mechanical interlocking, denoting hooking and twisting of irregularly shaped
particles.
The most common dominant bonding mechanisms for pharmaceutical materials are long
distance forces, especially van der Waals forces and hydrogen bonds in some cases. The
fundamentals for solid bridges are a relatively simple molecular structure and plastic
deformation. In order to form a coherent tablet, bonds between the particle contact
surfaces must be strong enough to withstand the elastic component of the material. The
final compact strength is dependent on many materials and process attributes. The tensile
strength of tablets is generally higher if the particle size is smaller (4). If the material
undergoes fragmentation during volume reduction, the particle size and shape will have a
minor effect on tablet strength.
Poor compactibility of powders, weak bonds between particles, or extensive elastic
relaxation of materials can decrease tablet strength and increase the capping tendency.
Capping is a phenomenon whereby extensive elastic relaxation breaks bonds that were
formed during compression, leading to laminar breakage of the upper part of the tablet.
Capping increases with increasing compression pressure, tableting speed, and tablet
thickness, as well as low powder humidity (5). Using precompression before the main
compression during tableting can lead to lower capping incidence (6).
The solid-state material properties, surface free energy, and structural changes have
important influence on powder compression behavior. The existence of polymorphism
and the degree of material crystallinity can have a significant impact on the tablet
properties. During compaction, mechanical energy can cause surfaces to become
disordered and activated, which can cause more intensive bonding (7).
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 304
11.1. Direct compression:
In early days, most of the tablets require granulation of the powdered Active
Pharmaceutical Ingredient (API) and Excipients. The availability of new excipients or
modified form of old excipients and the invention of new tablet machinery or
modification of old tablet machinery provides an ease in manufacturing of tablets by
simple procedure of direct compression.
Amongst the techniques used to prepare tablets, direct compression is the most advanced
technology. It involves only blending and compression. Thus offering advantage
particularly in terms of speedy production. Because it requires fewer unit operations, less
machinery, reduced number of personnel and considerably less processing time along
with increased product stability.
Tablet manufacturing by direct compression has increased steadily over the years. It
offers advantages over the other manufacturing processes for tablets, such as wet
granulation and provides high efficiency (7).As direct compression is more economic,
reducing the cycle time and straight forward in terms of good manufacturing practice
requirements. On the other hand wet granulation not only increases the cycle time, but
also has certain limits imposed by thermolability and moisture sensitivity of the active
drug substances. Therefore pharmaceutical industry is now focusing increasingly on the
direct compression process (8-9). Tablets produced by direct compression method give
lower microbial levels than those prepared by the wet granulation method. The
compaction process exerts lethal effect on the survival of microorganisms (10). The
tablets prepared by direct compression disintegrate into API particles instead of granules
that directly come into contact with the dissolution fluid and exhibit a comparatively
faster dissolution (11). The direct compression is a process of applying pressure (via an
upper and a lower punch) to materials held in a die cavity. The events that occur in the
process of compression are (12)
1. Transitional repacking.
2. Deformation at point of contact.
3. Fragmentation and/or deformation.
4. Bonding.
5. Deformation of the solid body.
6. Decompression.
7. Ejection.
The term ―direct compression‖ is defined as the process by which tablets are compressed
directly from powder mixture of API and suitable excipients. No pretreatment of the
powder blend by wet or dry granulation procedure is required. The events that motivate
the industry people to use direct compression technique is commercial availability of the
directly compressible excipients possessing both good compressibility and good
flowability. Terashita and Imamura in 2002 suggested that direct compression is able to
produce tablets at a lower cost than wet granulation and tableting method, due to a fewer
items of process validation. (13)
11.1.1. Merits of direct compression:
1. Direct compression is more efficient and economical process as compared to other
processes, because it involves only dry blending and compaction of API and
necessary excipients.
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 305
2. The most important advantage of direct compression is cost effectiveness. It is due to
reduced processing times, reduced labor costs, fewer manufacturing steps, and less
number of equipments are required, less process validation and reduced consumption
of power.
3. Elimination of heat and moisture, thus increasing not only the stability but also the
suitability of the process for thermolabile and moisture sensitive API’s.
4. Particle size uniformity.
5. Prime particle dissolution. In case of directly compressed tablets after disintegration,
each primary drug particle is liberated. While in the case of tablets prepared by
compression of granules, small drug particles with a larger surface area adhere
together into larger agglomerates; thus decreasing the surface area available for
dissolution.
6. The chances of batch-to-batch variation are negligible, because the unit operations
required for manufacturing processes is fewer.
7. Chemical stability problems for API and excipient would be avoided.
8. Provides stability against the effect of aging which affects the dissolution rates.
11.1.2. Merits of direct compression over wet granulation process:
The variables used in the processing of the granules can lead to significant tableting
problems. Properties of granules formed can be affected by viscosity of granulating
solution, the rate of addition of granulating solution, type of mixer used and duration of
mixing, method and rate of dry and wet blending. The above variables can change the
density and the particle size of the resulting granules and may have a major influence on
fill weight and compaction qualities. Drying can lead to unblending as soluble API
migrates to the surface of the drying granules.
11.1.3. Demerits
11.1.3.1. Excipient related demerits 1. Problems in the uniform distribution of low dose drugs.
2. High dose drugs having high bulk volume, poor compressibility and poor flowability
are not suitable for direct compression.
3. The choice of excipients for direct compression is extremely critical. Direct
compression diluents and binders must possess both good compressibility and good
flowability.
4. Many active ingredients are not compressible either in crystalline or amorphous
forms.
5. Direct compression blends may lead to unblending because of difference in particle
size or density of drug and excipients. Similarly the lack of moisture may give rise to
static charges, which may lead to unblending.
6. Non-uniform distribution of colour, especially in tablets of deep colours.
11.1.3.2. Process related demerits 1. Capping, lamination, splitting, or layering of tablets is sometimes related to air
entrapment during direct compression. When air is trapped, the resulting tablets
expand when the pressure of tablet is released, resulting in splits or layers in the
tablet.
2. In some cases require greater sophistication in blending and compression
equipments.
3. Direct compression equipments are expensive.
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 306
11.1.4. Manufacturing steps for direct compression
Direct compression involves comparatively few steps:
1. Milling of drug and excipients.
2. Mixing of drug and excipients.
3. Tablet compression.
Figure: 11.1. Manufacturing Steps for Direct Compression.
11.1.5. Direct compression Excipients:
Direct compression excipients mainly include diluents, binders and disintegrants.
Generally these are common materials that have been modified during the chemical
manufacturing process, in such a way to improve compressibility and flowability of the
material. The physicochemical properties of the ingredients such as particle size,
flowability and moisture are critical in direct compression tableting. The success of direct
compression formulation is highly dependent on functional behavior of excipients.
11.1.5.1. Ideal properties of directly compressible excipients
1. It should have good compressibility.
2. It should possess good hardness after compression, that is material should not
possess any deformational properties; otherwise this may lead to capping and
lamination of tablets.
3. It should have good flowability.
4. It should be physiologically inert.
5. It should be compatible with wide range of API.
6. It should be stable to various environmental conditions (air, moisture, heat, etc.).
7. It should not show any physical or chemical change in its properties on aging.
8. It should have high dilution potential. i.e. able to incorporate high amount of API.
9. It should be colorless, odorless and tasteless.
10. It should accept colorants uniformity.
11. It should possess suitable organoleptic properties according to formulation type, i.e.
in case of chewable tablet diluents should have suitable taste and flavor. For example
mannitol produces cooling sensation in mouth and also sweet taste.
12. It should not interfere with bioavailability and biological activity of active
ingredients.
13. It should be easily available and economical in cost.
11.1.5.2. Ideal Properties of API for direct tabetting:
1. Absence of static charge on surface
2. Good compatibility with excipients
3. Good compressibility
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 307
4. Good flowability
5. Good organoleptic properties
6. High Purity
7. High stability
8. Optimum and Uniform particle size-particle size distribution
9. Optimum bulk powder properties
10. Optimum moisture content
11. Spherical shape
11.2. Procedure for preparation of directly compressible tablet: The tablets of macrolide antibiotics and optimized recrystallized agglomerates were
prepared by direct compression method. The following steps are involved in preparation
of tablets
Raw material dispensing and sifting: Dispense the raw materials as per mentioned in
individual formula for formulation of tablets.
Sifting: Sift all inactive ingredients through sieve no #30
Mixing: Mix macrolide antibiotics or prepared recrystallized agglomerates as mentioned
in formula with diluents for five minutes in polybag.
Prelubrication: To the above mixed blend added sifted quantity of super disintegrant
Crosscarmelose Sodium (AC-Di-Sol) and talc and continue mixing for 3 minutes.
Lubrication: To the above pre lubricated blend added sifted quantity of magnesium
stearate and mix for few minutes in polybag.
Flow rate determination:
Physical properties such as bulk density, tapped density, compressibility index, Hausnar
ratio and the angle of repose of blend were determined to evaluate the flow of lubricated
blend.
Compression:
The lubricated blend for average weight per unit tablet as mentioned below table:11.1
was Compressed by using KBR Press with flate type punches and die (diameter 13mm)
for azithromycin, clarithromycin and by using 8-station compression machine with
standard concave type punches and die(9.5mm) for roxithromycin and erythromycin
which are lubricated with 0.5% magnesium stearate.
Table: 11.1. Average weights of macrolide antibiotics tablets with their respective
strength. Sr.No. Name of tablet Average weight(mg)
01 Azithromycin 500mg tablet 700-750
02 Clarithromycin 500mg tablet 700-760
03 Roxithromycin 300mg tablet 440-480
04 Erythromycin 250mg tablet 350-381
11.3. Evaluation of tablets:
11.3.1. Assay (drug content):
Single tablet of macrolide antibiotic was weighed and powdered .The powder was
weighed equivalent to 50mg of macrolide antibiotics and diluted to 60ml with 0.1N HCl,
adjusted the pH 6 to 7 by adding 0.4M NaOH solution and made up the volume up to
100ml with distilled water. 1ml form the above solution was diluted to 6 ml with the
distilled water in 10 ml volumetric flask and to it added Eosin Y solution (4 X 10-3
M) (
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 308
Azithromycin-0.5ml,Clarithromycin-1.2ml,Roxithromycin-0.7ml and Erythromycin-
0.7ml), mixed well and to it added 1 ml 0.4M acetate buffer (pH 3) adjust the volume up
to 10ml with distilled water. The absorbance was measured spectrophotometrically at
544.5nm, 542.5nm, 545nm, 547nm for Erythromycin, Roxithromycin, Clarithromycin
and Azithromycin respectively against an appropriate blank prepared simultaneously.
Content of macrolide antibiotics were determined either the calibration graph by using
the corresponding regression equation.(14)
11.3.2. Content uniformity:
Determine the content of macrolide antibiotics in each of 10 tablets as per above
analytical procedure mentioned in drug content determination. The tablet complies with
the test if each individual content is 85-115% of the average content. The tablet fails to
comply the test if more than one individual content is out side theses limits or if one
individual content is outside the limit of 75-125% of the average content. (15)
11.3.3. Thickness, length and width measurement:
The thickness of a tablet was determined by the amount of fill permitted to enter the die
and the amount of pressure applied during compression (16). Five tablets were taken and
their thickness, length and width were determined individually by vernier caliper. Mean
and standard deviation were calculated.
11.3.4. Crushing strength or hardness determination:
Five tablets were taken randomly and hardness was measured using Hardness Tester
(Pfizer hardness tester).
11.3.5. Friability:
For tablet with an average weight of 650mg or less take a sample of whole tablets
corresponding to about 6.5 gm and for tablet with an average weight of more than 650mg
take sample of 10 whole tablets.
As the average weight of Azithromycin and Clarithromycin tablet was above 650mg take
whole 10 tablets for the study. In case of roxithromycin and erythromycin the average
weight of tablets was below 650mg therefore take 15 and 20 tablets of roxithromycin and
erythromycin for friability study.
Dedust the tablets carefully and weigh accurately the required number of tablets for the
study as per above mentioned number of tablets selection condition. Place the tablets in
the drum of Roche friabilator apparatus and rotate it for 100 times or rotated at 25 rpm
for 4 minutes. Remove the tablets and any loose dust from them and weigh accurately
after revolving the tablets. The percentage friability was measured using the formula,
Where %F = Friability in percentage.
W0 = Initial weight of tablets.
W = Weight of tablet after revolution.
A maximum loss of weight was not greater than 1.0 % which is acceptable for most
tablets. If one or more tablets were cracked, chipped or broken during the test the tablets
fails the friability test as per Indian Pharmacopoeia. If the size and shape of tablets causes
irregular tumbling, adjust the drum base so that it forms an angle of about 100 with the
horizontal and tablets do not binds together when lying next to each other. (17)
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 309
11.3.6. Weight variation:
The variation in weight of individual tablets is a valid indication of the corresponding
variation in the drug content (18). The average tablet weight was determined by weighing
20 units of tablets individually using an analytical balance. Weigh the average weight of
20 tablets and than weigh individually 20 tablets on analytical balance. Not less than two
of the individual weight deviates from the average weight by more than the % shown in
the table: 12.2.
Table: 11.2. Limits of percentage deviation of weight in weight variation study of
tablets. Sr.No. Average weight (mg) % Deviation
1 80 or less 10
2 80-250 7.5
3 250 or more 5
11.3.7. Tablet elastic recovery test: Place the powder blend equivalent to average weight of samples in 13.0 mm die for
azithromycin, clarithromycin and in 9.5 mm die for roxithromycin, erythromycin and
compress by using KBr Press. Measure the thickness of compacted tablet under
maximum pressure (HC) and 24 hrs after tablet ejection (He).The following equation was
used to calculate the elastic recovery ratio(ER) (19)
ER = [(He – Hc) / Hc] X100
11.3.8. Tensile strength:
Plastic deformation of agglomerates having porous structure and lower crystallinity,
during compression might be responsible for increasing the interparticle bonding in a
tablet. (20) The tensile strength of tablet (T) was calculated using the following formula,
T = 2F / π DL.
Where, T = Tablet tensile strength.
D = Tablet diameter (mm).
L = Thickness (mm).
F = Hardness (Kg/cm2).
11.3.9. Porosity of tablet:
Twenty-four hours after ejection of compacted tablet of macrolide antibiotics and their
agglomerated crystals, measured the volume of the compacted tablet by measuring
thickness and diameter (19).
The %Porosity (ε) was calculated from the following equation.
ε = {(v-vo) / v} Χ 100
Where, v = Tablet volume(r Χ h.)
r = Radius of the compacted tablet.
h = thickness of the compacted tablet.
vo = the volume of material at zero porosity (true volume)
11.3.10. Wetting Time and Water Absorption Ratio:
A piece of tissue paper folded twice was kept in a culture dish (internal diameter 5.5 cm)
containing ≈6 mL of purified water. A tablet having a small amount of amaranth powder
on the upper surface was placed on the tissue paper. The time required to develop a red
color on the upper surface of the tablet was recorded as the wetting time. The same
procedure without amaranth was followed for determining the water absorption ratio
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 310
(21). The wetted tablet was weighed and the water absorption ratio, R, was determined
according to the following equation,
Where Wb and Wa were the weights of the tablet before and after study.
11.3.11. Disintegration time:
Disintegration is evaluated to ensure that the drug substance is fully available for
dissolution and absorption from the gastrointestinal tract (22).The test determines
whether tablet disintegrate with in the prescribed time when placed in liquid medium
under the prescribed condition. Disintegration test was carried out as described under
procedure for uncoated tablets in IP.Introduce one tablet into each tube and kept disc
above the tablet in each tube. Suspend the assembly in the beaker containing 900mL
purified water as the immersion fluid at 37 ± 20C for specified time period. Remove the
assembly from the liquid, the time required for complete disintegration was noted for
each tablet. Tablet passes the test if all of them have disintegrated. If one or two tablets
fails to disintegrate, repeat the test on additional 12 tablets, not less than 16 of the total 18
tablets tested disintegrate.
11.3.12. Dissolution study:
The in vitro dissolution studies were carried out using eight station USP type II
dissolution apparatus. The study was carried out in 900 ml of dissolution medium as per
mentioned in below table: 11.3. Dissolution medium was kept in a thermostatically
controlled water bath, maintained at 37±0.50C.The paddle was rotated at 50-100 rpm as
per mentioned in table. At predetermined time intervals, 5ml of samples were withdrawn
and assessed for drug release spectrophotometrically. At each withdrawal, 5ml of fresh
dissolution medium was added to dissolution jar so as to maintain sink condition. 1ml
quantity of withdraw sample was taken into 10ml volumetric flask and diluted to 6ml
with distilled water. Eosin Y solution (4 X 10-3
M) was added (Azithromycin-
0.5ml,Clarithromycin-1.2ml,Roxithromycin-0.7ml and Erythromycin-0.7ml) and mixed
well than to it added 1 ml 0.4M acetate buffer (pH 3) and adjusted the volume up to 10ml
with distilled water. The absorbance was measured spectrophotometrically at 540.5nm,
542.5nm, 540nm, 544nm for Azithromycin, Clarithromycin, Roxithromycin and
Erythromycin respectively against an appropriate blank prepared simultaneously.
In vitro release was demonstrated by comparison of the dissolution profile after fitting
into the mathematical model, similarity factor, f2. The similarity factor, f2 used as the
mathematical model for comparing the dissolution profile.
Where, f2 = Similarity factor; n = Number of time points; R (t) = Mean percent drug
dissolved e.g. a reference product; T (t) = Mean percent drug dissolved of e.g. a test
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 311
product. Not more than one mean value of >85% dissolved for each formulation. An f2
value between 50 and 100 suggests that the two dissolution profiles are similar12.
Table: 11.3. Dissolution conditions of tablets prepared from macrolide antibiotics
and their optimized recrystallized agglomerates. Macrolide
Antibiotics
App: Speed Volume Medium
Azithromycin App-II (Paddle) 75rpm 900ml 0.1M Phosphate buffer pH 6.0
Clarithromycin App-II (Paddle) 50rpm 900ml 0.1M Sodium Acetate buffer pH 5.0
Roxithromycin App-II (Paddle) 100rpm 900ml Acetate buffer pH 5.0
Erythromycin App-II (Paddle) 50rpm 900ml 0.05M pH 6.8 phosphate buffer
Table: 11.4. Marketed tablets of macrolide antibiotics used for comparative study. Macrolide
antibiotics
Marketed tablet Tablet code Strength
(mg)
Weight
(mg)
Description of Tablet.
Azithromycin Zathrin Tablet
(FDC Ltd.)
ATM(m)-Tab 500mg 760mg Pink colored capsule shaped
tablet plain on both side
Clarithromycin Claribid Tablet
(Pfizer Ltd.)
CTM(m)-Tab 500mg 790mg Oval shaped yellow colored
tablet
Roxithromycin Roxid Tablet
(Alembic Ltd.)
RTM(m)-Tab 300mg 870mg Capsule shaped pink colored
tablet having one sided beak line
and plain on other side
Erythromycin Althrocin Tablet
(Alembic Ltd.)
ETM(m)-Tab 250mg 500mg White round shaped tablet having
Althrocin and 250 embossing
with break line which bifurcate
the Althrocin and 250 embossing
on one side and plain on other
side.
Table: 11.5. Evaluation parameters of macrolide antibiotics marketed tablets used for
comparative study. Marketed tablet Shape Diameter(mm) Thickness(mm) Length(mm) Width(mm)
Zathrin Tablet
(FDC Ltd.)
Capsule NA 6.00 19.00 10.00
Claribid Tablet
(Pfizer Ltd.)
Oval NA 7.00 19.00 9.00
Roxid Tablet
(Alembic Ltd.)
Capsule NA 7.00 17.00 8.00
Althrocin Tablet
(Alembic Ltd.)
round 12.00 4.00 NA NA
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 312
Figure: 11.2. Shape and packing of marketed macrolide antibiotics tablets taken for
comparative study.
Table: 11.4, 11.5 represent the evaluation parameters like physical description, weight,
shape, strength, shape and size and figure: 11.2 represent the photographs of marketed
macrolide antibiotics tablets for comparative purpose. For comparative purpose the
marketed strength of 500mg, 500mg, 300mg and 250mg for azithromycin,
clarithromycin, roxithromycin and erythromycin tablets were taken. The respective
weight of the taken marketed strength was given in table: 11.4.
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 313
11.4. Formulation, preparation and evaluation of Azithromycin tablet:
Table: 11.6. Tablet formulations of ATM and their optimized recrystallized
agglomerates.
Sr.
No: Name of ingredients
Quantity(mg)
ATM-
Tab
ATME-
Tab
ATMP-
Tab
ATMS-
Tab
ATMN-
Tab
1 ATM 500 ----- ----- ----- -----
2 ATM- EudS (equiv.) ----- 543 ----- ----- -----
3 ATM-PVP ----- ----- 543 ----- -----
4 ATM-SSG ----- ----- ----- 549 -----
5 ATM-N(HPMC) ----- ----- ----- ----- 543
6 Dibasic Calcium Phosphate 75 75 75 75 75
7 Microcrystalline
cellulose(Avicel pH 102) 100 100 100 100 100
8 Crosscarmelose
Sodium(AC-Di-Sol) 20 20 20 20 20
9 Talc 2.5 2.5 2.5 2.5 2.5
10 Magnesium Stearate 2.5 2.5 2.5 2.5 2.5
Total weight (mg) 700 743 743 749 743
Table: 11.7. Evaluation of lubricated blend of ATM and their optimized
recrystallized agglomerates.
Sr.
No Evaluation parameters
Tablet code
ATM-
Tab
ATME-
Tab
ATMP-
Tab
ATMS-
Tab
ATMN-
Tab
1 Bulk density (gm/mL) 0.667 0.333 0.333 0.313 0.313
2 Tap density (gm/mL) 0.833 0.385 0.400 0.370 0.376
3 Compressibility index (CI) 20 13.33 16.66 15.625 16.88
4 Hausner’s ratio 1.25 1.15 1.20 1.19 1.20
5 Angle of repose (Degree) 28 18 20 21 23
6 Flow rate (gm/sec) 0.25 0.71 0.50 0.62 0.55
Table: 11.8. Weight variation studies of azithromycin tablets.
Tablet no Weight in mg (% deviation)
ATM-Tab ATME-Tab ATMP-
Tab
ATMS-Tab ATMN-Tab
1 685(2.7) 740(0.1) 735(0.8) 750(0.1) 737(0.5)
2 725(3.0) 735(0.6) 737(0.5) 755(0.5) 745(0.5)
3 741(5.2) 732(1.0) 745(0.6) 747(0.5) 742(0.1)
4 725(3.0) 737(0.3) 745(0.6) 753(0.3) 741(0.0)
5 680(3.4) 734(0.7) 738(0.4) 752(0.1) 742(0.0)
6 666(5.4) 729(1.4) 740(0.1) 750(0.1) 742(0.1)
7 722(2.5) 751(1.6) 742(0.2) 749(0.3) 742(0.1)
8 675(4.1) 746(0.9) 743(0.3) 748(0.4) 740(0.1)
9 705(0.1) 742(0.4) 742(0.2) 754(0.4) 739(0.3)
10 709(0.7) 745(0.8) 741(0.0) 751(0.0) 740(0.1)
Avg.weight
(mg) 704.1 739.1 740.8 750.9 741
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 314
Table: 11.9. Content uniformity study of Azithromycin tablet.
Tablet
no.
Concentration (%)
ATM-Tab ATME-Tab ATMP-Tab ATMS-Tab ATMN-Tab
1 95 93 97 98 93
2 90 95 94 92 95
3 88 97 103 95 97
4 115 92 92 96 94
5 107 90 90 97 95
6 108 88 93 94 98
7 112 103 94 95 92
8 94 97 96 95 93
9 87 95 98 96 97
10 83 96 93 98 90
Avg 97.9 94.6 95 95.6 94.4
Min. 83 88 90 92 90
Max. 115 103 103 98 98
SD 11.55 4.20 3.68 1.84 2.50
%SD 11.80 4.43 3.88 1.92 2.65
Table: 11.10. Evaluation of tablets prepared from ATM and their optimized
recrystallized agglomerates.
Sr.No: Evaluation parameters
Tablet Code
ATM-
Tab
ATME-
Tab
ATMP-
Tab
ATMS-
Tab
ATM
N-Tab
ATM(m)
-Tab
1 Description
2 Assay (Drug content) 95 93 94 97 95 95
3 Thickness (mm) 6.0 5.4 5.8 5.4 5.2 8.0
4 Hardness (kg) 4.5 7.0 6.2 8.5 5.8 6.5
5 Friability 1.75 0.72 0.45 0.65 0.61 0.56
6 Tensile strength 0.037 0.064 0.052 0.077 0.055 NA 7 Porosity of tablet 1.67 5.56 6.90 3.70 7.69 NA 8 Elastic recovery 5.00 3.64 3.45 3.70 3.85 NA
9 Wetting Time(Minutes) 9 5 6 4 5 6
10 Water Absorption Ratio ( R ) 34 39 42 46 40 38
11 Disintegration time (min.) 5-6 6-7 5-6 3-4 4-5 3-4
12 Dissolution % Cumulative drug release (%CDR)
Dissolution condition:
Medium:0.1M Phosphate
buffer pH 6.0, 900ml ,
75rpm
USP App-II (Paddle)
5 Min. 48 61 57 62 58 53
15 Min. 57 74 68 70 72 61
30 Min. 64 82 78 81 84 71
45 Min. 74 88 85 89 92 84
60 Min. 82 96 94 97 97 94
F2 values (Ref:ATM-Tab) NA 48.17 54.30 48.83 47.29 61.59
F2 values (Ref:ATM(m)-Tab) 61.59 60.39 72.58 62.86 60.0 NA
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 315
Wetting time and water absorption ratio of Azithromycin tablet
0
10
20
30
40
50
ATM-Tab ATME-Tab ATMP-Tab ATMS-Tab ATMN-Tab ATM(m)-Tab
Wetting Time(min) Water Absorption Ratio ( R )
Figure: 11.3. Wetting time and water absorption ratio of tablets prepared from
ATM and their recrystallized agglomerates.
Dissolution profile of Azithromycin tablet
0
20
40
60
80
100
0 10 20 30 40 50 60
Time(min.)
%C
DR
ATM-Tab ATME-Tab ATMP-Tab
ATMS-Tab ATMN-Tab ATM(m)-Tab
Figure: 11.4. Comparative dissolution studies of prepared azithromycin tablet with
optimized recrystallized agglomerates and marketed tablet.
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 316
11.5. Formulation, preparation and evaluation of Clarithromycin tablet:
Table: 11.11. Tablet formulations of CTM and their optimized recrystallized
agglomerates.
Sr.N
o: Name of ingredients
Quantity(mg)
CTM-Tab CTME –
Tab
CTMP –
Tab
CTMS -
Tab
CTMN-
Tab
1 CTM 500 ----- ----- ----- -----
2 CTM- EudS(equiv.) ----- 556 ----- ----- -----
3 CTM-PVP ----- ----- 538 ----- -----
4 CTM-SSG ----- ----- ----- 556 -----
5 CTM-N(HPMC) ----- ----- ----- ----- 556
6 Microcrystalline
Cellulose(Avicel pH 102) 175 175 175 175 175
8 Crosscarmelose Sodium(AC-
Di-Sol) 20 20 20 20 20
9 Talc 2.5 2.5 2.5 2.5 2.5
10 Magnesium Stearate 2.5 2.5 2.5 2.5 2.5
Total weight (mg) 700 756 738 756 756
Table: 11.12. Evaluation of lubricated blend of CTM and their optimized recrystallized
agglomerates.
Sr.
No:
Evaluation
parameters
Tablet code
CTM-Tab CTME –Tab CTMP –Tab CTMS -Tab CTMN-Tab
1 Bulk density
(gm/mL) 0.455 0.294 0.313 0.303 0.278
2 Tap density
(gm/mL) 0.588 0.345 0.370 0.345 0.333
3 Compressibility
index (CI) 22.72 14.71 15.62 12.12 16.67
4 Hausner’s ratio 1.29 1.17 1.18 1.14 1.20
5 Angle of repose
(Degree) 30 23 24 21 24
6 Flow rate
(gm/sec) 0.06 2.50 1.30 0.63 0.50
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 317
Table: 11.13. Weight variation studies of Clarithromycin tablets.
Tablet no Weight in mg (% deviation)
CTM-Tab CTME –Tab CTMP –Tab CTMS -Tab CTMN-Tab
1 722(2.6) 740(0.0) 747(0.9) 755(0.5) 746(0.6)
2 713(1.3) 742(0.3) 735(0.7) 757(0.8) 750(0.0)
3 695(1.3) 747(1.0) 736(0.6) 753(0.2) 754(0.5)
4 729(3.6) 733(0.9) 738(0.3) 745(0.8) 756(0.8)
5 737(4.7) 735(0.6) 740(0.1) 747(0.6) 758(1.0)
6 740(5.1) 737(0.4) 742(0.2) 748(0.4) 760(1.3)
7 667(5.2) 740(0.0) 743(0.3) 744(1.0) 742(1.1)
8 685(2.7) 740(0.0) 740(0.1) 752(0.1) 741(1.2)
9 675(4.1) 744(0.6) 738(0.3) 755(0.5) 754(0.5)
10 675(4.1) 739(1.0) 746(0.7) 757(0.8) 742(1.1)
Avg.weight
(mg) 703.8 739.7 740.5 751.3 750.3
Table: 11.14. Content uniformity study of Clarithromycin tablet.
Tablet
no.
Concentration (%)
CTM-Tab CTME –Tab CTMP –Tab CTMS -Tab CTMN-Tab
1 98 95 97 94 93
2 92 97 94 97 96
3 95 94 93 95 98
4 86 95 95 96 98
5 82 98 96 97 96
6 97 96 97 97 95
7 99 94 97 97 97
8 85 93 97 93 96
9 105 94 95 94 94
10 107 95 94 95 98
Avg 94.6 95.1 95.5 95.5 96.1
Min. 82 93 93 93 93
Max. 107 98 97 97 98
SD 8.37 1.52 1.51 1.51 1.73
%SD 8.85 1.60 1.58 1.58 1.80
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 318
Table: 11.15. Evaluation of tablets prepared from CTM and their optimized
recrystallized agglomerates.
Sr.No Evaluation parameters
Tablet Code
CTM-
Tab
CTME –
Tab
CTMP
–Tab
CTMS
-Tab
CTMN-
Tab
CTM(m)-
Tab
1 Description
2 Assay (Drug content) 96 95 97 98 96 98
3 Thickness(mm) 5.9 5.5 5.3 5.4 5.7 8.5
4 Hardness(kg) 5 8 7 9 7 9
5 Friability 1.17 0.42 0.41 0.51 0.48 0.58
6 Tensile strength 0.042 0.071 0.065 0.082 0.060 NA
7 Porosity of tablet 3.39 7.27 5.66 5.56 7.02 NA
8 Elastic recovery 8.47 3.64 3.77 3.70 5.26 NA
9 Wetting Time(hrs) 8 4 5 3 4 6
10 Water Absorption Ratio
( R ) 23 38 35 40 37 32
11 Disintegration
time(minutes) 5-6 4-5 5-6 3-4 4-5 3-4
12 Dissolution % Cumulative drug release (%CDR)
Medium: 0.1M Sodium
Acetate,buffer pH
5.0,900ml, 50rpm,
USP App-II (Paddle)
5 Min. 27 51 47 52 48 40
15 Min. 40 65 63 68 66 59
30 Min. 47 76 78 79 76 67
45 Min. 58 86 83 86 83 80
60 Min. 70 95 93 96 94 87
F2 values (Ref:CTM-Tab) NA 36.52 37.88 35.22 37.48 44.16
F2 values (Ref:CTM(m)-Tab) 44.16 61.46 65.45 57.61 64.54 NA
Wetting time and water absorption ratio of Clarithromycin tablet
0
10
20
30
40
50
CTM-Tab CTME –Tab CTMP –Tab CTMS -Tab CTMN-Tab CTM(m)-Tab
Wetting Time(min) Water Absorption Ratio ( R )
Figure: 11.5. Wetting time and water absorption ratio of tablets prepared from
CTM and their recrystallized agglomerates.
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 319
Dissolution profile of Clarithromycin tablet
0
20
40
60
80
100
0 10 20 30 40 50 60
Time(min.)
%C
DR
CTM-Tab CTME-Tab CTMP-Tab
CTMS-Tab CTMN-Tab CTM(m)-Tab
Figure: 11.6. Comparative dissolution studies of prepared clarithromycin tablet
with optimized recrystallized agglomerates and marketed tablet.
11.6. Formulation, preparation and evaluation of Roxithromycin tablet:
Table: 11.16. Tablet formulation of RTM and their optimized recrystallized
agglomerates.
Sr.No: Name of ingredients
Quantity(mg)
RTM-
Tab
RTMH-
Tab
RTMP-
Tab
RTMS-
Tab
RTMN-
Tab
1 RTM 300 ----- ----- ----- -----
2 RTM- HPC(equiv.) ----- 330 ----- ----- -----
3 RTM-PVP ----- ----- 326 ----- -----
4 RTM-SSG ----- ----- ----- 330 -----
5 RTM-N(HPMC) ----- ----- ----- ----- 337
6 Microcrystalline
Cellulose (Avicel) 72 72 72 72 72
7 Lactose 44 44 44 44 44
8 Crosscarmelose
Sodium(AC-Di-Sol) 20 20 20 20 20
9 Magnesium Stearate 4 4 4 4 4
Total weight (mg) 440 470 466 470 477
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 320
Table: 11.17. Evaluation of lubricated blend of RTM and their optimized
recrystallized agglomerates.
Sr.No.
Evaluation
parameters
Tablet code
RTM-
Tab
RTMH-Tab RTMP-Tab RTMS-Tab RTMN-Tab
1 Bulk density
(gm/mL) 0.667 0.357 0.352 0.333 0.333
2 Tap density
(gm/mL) 0.833 0.417 0.410 0.379 0.397
3 Compressibility
index (CI) 20 14.28 14.08 12.00 16.00
4 Hausner’s ratio 1.25 1.17 1.16 1.14 1.19
5 Angle of repose
(Degree) 27 23 22 24 25
6 Flow rate
(gm/sec) 0.33 0.50 0.63 0.71 0.42
Table: 11.18. Weight variation studies of Roxithromycin tablets. Tablet no Weight in mg (% deviation)
RTM-Tab RTMH-Tab RTMP-Tab RTMS-Tab RTMN-Tab
1 445(1.0) 471(0.0) 465(0.0) 474(0.3) 482(0.6)
2 447(1.4) 470(0.2) 462(0.7) 475(0.5) 483(0.8)
3 446(1.2) 468(0.6) 467(0.4) 473(0.0) 479(0.0)
4 442(0.3) 472(0.2) 465(0.0) 472(0.2) 476(0.6)
5 437(0.8) 472(0.2) 465(0.0) 471(0.4) 477(0.4)
6 434(1.5) 473(0.4) 466(0.2) 470(0.6) 478(0.2)
7 433(1.7) 471(0.0) 464(0.3) 470(0.6) 479(0.0)
8 438(0.6) 468(0.6) 467(0.4) 472(0.2) 482(0.6)
9 440(0.2) 474(0.7) 466(0.2) 475(0.5) 473(1.3)
10 445(1.0) 470(0.2) 465(0.0) 476(0.7) 482(0.6)
Avg.weight
(mg) 440.7 470.9 465.2 472.8 479.1
Table: 11.19. Content uniformity study of Roxithromycin tablet. Tablet
no.
Concentration (%)
RTM-Tab RTMH-Tab RTMP-Tab RTMS-Tab RTMN-Tab
1 93 96 94 95 95
2 96 97 97 96 96
3 95 95 95 92 94
4 91 94 95 94 96
5 94 95 96 95 95
6 97 95 98 98 94
7 96 95 95 95 96
8 92 98 99 96 95
9 98 95 94 95 94
10 93 98 95 95 97
Avg 94.5 95.8 95.8 95.1 95.2
Min. 91 94 94 92 94
Max. 98 98 99 98 97
SD 2.27 1.40 1.69 1.52 1.03
%SD 2.41 1.46 1.76 1.60 1.08
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 321
Table: 11.20.Evaluation of tablets prepared from RTM and their optimized
recrystallized agglomerates.
Sr.No: Evaluation parameters
Tablet Code
RTM-
Tab
RTMH-
Tab
RTMP-
Tab
RTMS-
Tab
RTMN-
Tab
RTM(m)
-Tab
1 Description
2 Assay (Drug content) 96 98 96 95 96 95
3 Thickness(mm) 6 5.7 5.6 5.6 5.7 7.0
4 Hardness(kg) 3 5 6 5 7 8
5 Friability 1.29 0.26 0.62 0.52 0.34 0.48
6 Tensile strength 0.034 0.059 0.072 0.060 0.082 NA
7 Porosity of tablet 3.33 5.26 5.36 7.14 7.02 NA
8 Elastic recovery 6.67 3.51 3.57 3.57 3.51 NA
9 Wetting Time(hrs) 8 5 5 4 6 7
10 Water Absorption Ratio
( R ) 27 37 35 42 37 32
11 Disintegration time
(minutes) 3-4 2-3 2-3 1-2 3-4 2-3
12 Dissolution % Cumulative drug release (%CDR)
Medium: Acetate
buffer pH 5.0,
900ml, 100rpm,USP
App-II (Paddle)
5 Min. 32 45 47 50 48 43
15 Min. 47 53 56 61 58 58
30 Min. 55 68 71 74 72 70
45 Min. 63 81 84 85 83 79
60 Min. 74 92 94 96 93 90
F2 values (Ref:RTM-Tab) NA 49.66 46.25 43.27 46.06 50.12
F2 values (Ref:RTM(m)-Tab) 50.12 82.31 78.57 70.17 79.85 NA
Wetting time and water absorption ratio of Roxithromycin tablet
0
10
20
30
40
50
RTM-Tab RTMH-Tab RTMP-Tab RTMS-Tab RTMN-Tab RTM(m)-Tab
Wetting Time(min) Water Absorption Ratio ( R )
Figure: 11.7. Wetting time and water absorption ratio of tablets prepared from
RTM and their recrystallized agglomerates.
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 322
Dissolution profile of Roxithromycin tablet
0
20
40
60
80
100
0 10 20 30 40 50 60
Time(min.)
%C
DR
RTM-Tab RTMH-Tab RTMP-Tab
RTMS-Tab RTMN-Tab RTM(m)-Tab
Figure: 11.8. Comparative dissolution studies of prepared roxithromycin tablet with
optimized recrystallized agglomerates and marketed tablet.
11.7. Formulation, preparation and evaluation of Erythromycin tablet:
Table: 11.21. Tablet formulations of ETM and their optimized recrystallized
agglomerates.
Sr.No: Name of ingredients
Quantity(mg)
ETM-
Tab
ETME-
Tab
ETMB-
Tab
ETMS-
Tab
ETMN-
Tab
1 ETM 250 ----- ----- ----- -----
2 ETM-EudS(equiv.) ----- 275 ----- ----- -----
3 ETM-BCD ----- ----- 278 ----- -----
4 ETM-SSG ----- ----- ----- 272 -----
5 ETM-N(HPMC) ----- ----- ----- ----- 281
6 Microcrystalline
Cellulose 58 58 58 58 58
7 Lactose 30 30 30 30 30
8 Crosscarmelose
Sodium(AC-Di-Sol) 10 10 10 10 10
9 Magnesium Stearate 2 2 2 2 2
Total weight (mg) 350 375 378 372 381
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 323
Table: 11.22. Evaluation of lubricated blend of ETM and their optimized
recrystallized agglomerates.
Sr.
No
Evaluation parameters
Tablet code
ETM-
Tab
ETME-
Tab
ETMB-
Tab
ETMS-
Tab
ETMN-
Tab
1 Bulk density
(gm/mL) 0.357 0.238 0.294 0.313 0.303
2 Tap density
(gm/mL) 0.455 0.263 0.345 0.370 0.362
3 Compressibility
index (CI) 21.43 9.52 14.71 15.63 16.36
4 Hausner’s ratio 1.27 1.11 1.17 1.18 1.19
5 Angle of repose
(Degree) 34 26 28 25 27
6 Flow rate
(gm/sec) 0.04 1.67 0.83 0.63 0.55
Table: 11.23.Weight variation studies of Erythromycin tablets. Tablet no Weight in mg (% deviation)
ETM-Tab ETME- Tab ETMB- Tab ETMS- Tab ETMN- Tab
1 335(5.5) 376(0.3) 382(0.9) 370(0.2) 381(0.1)
2 355(0.1) 380(1.4) 375(1.0) 375(1.5) 385(1.1)
3 365(2.9) 370(1.3) 377(0.4) 367(0.6) 376(1.2)
4 345(2.7) 372(0.7) 379(0.1) 368(0.4) 378(0.7)
5 360(1.5) 375(0.1) 380(0.4) 370(0.2) 380(0.2)
6 366(5.8) 376(0.3) 374(1.2) 366(0.9) 384(0.9)
7 347(2.1) 378(0.9) 378(0.2) 368(0.4) 384(0.9)
8 348(1.9) 380(1.4) 379(0.1) 370(0.2) 381(0.1)
9 360(1.5) 368(1.8) 382(0.9) 372(0.7) 378(0.7)
10 365(2.9) 373(0.5) 380(0.4) 368(0.4) 380(0.2)
Avg.weight
(mg) 355.5 374.8 378.6 369.4 380.7
Table: 11.24. Content uniformity study of Erythromycin tablet. Tablet
no.
Concentration (%)
ETM-Tab ETME- Tab ETMB- Tab ETMS- Tab ETMN- Tab
1 92 94 98 95 95
2 96 96 96 96 93
3 105 97 97 94 94
4 95 95 96 97 96
5 97 96 96 96 95
6 108 95 97 95 95
7 88 96 98 98 95
8 93 97 96 96 96
9 95 94 98 95 97
10 102 95 96 96 94
Avg 97.1 95.5 96.8 95.8 95
Min. 88 94 96 94 93
Max. 108 97 98 98 97
SD 6.15 1.08 0.92 1.14 1.15
%SD 6.34 1.13 0.95 1.19 1.22
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 324
Table: 11.25. Evaluation of tablets prepared from ETM and their optimized
recrystallized agglomerates.
Sr.No: Evaluation
parameters
Tablet Code
ETM-
Tab
ETME-
Tab
ETMB
- Tab
ETMS
- Tab
ETMN-
Tab
ETM(m)
- Tab
1 Description
2 Assay (Drug content) 95 96 98 97 95 95
3 Thickness(mm) 5.2 4.8 4.9 4.7 4.8 4.5
4 Hardness(kg) 3 4.2 4.5 5.0 4.4 5.0
5 Friability 1.27 0.41 0.22 0.65 0.55 0.35
6 Tensile strength 0.039 0.059 0.062 0.071 0.061 NA
7 Porosity of tablet 3.85 6.25 6.12 8.51 6.25 NA
8 Elastic recovery 7.69 4.17 4.08 6.38 4.17 NA
9 Wetting Time(min) 7 4 3 3 5 5
10 Water Absorption
Ratio ( R ) 25 34 31 45 38 35
11 Disintegration time 3-4 2-3 2-3 1-2 2-3 3-4
12 Dissolution % Cumulative drug release (%CDR)
Medium: 0.05M pH
6.8 phosphate
Buffer, 900ml,
50rpm
USP App-II
(Paddle).
5 Min. 28 40 42 48 46 35
15 Min. 40 58 57 62 60 47
30 Min. 52 72 68 71 74 62
45 Min. 60 84 78 82 83 78
60 Min. 74 94 90 95 96 92
F2 values (Ref:ETM-Tab) NA 43.30 46.90 41.54 41.29 51.69
F2 values (Ref:ETM(m)-Tab) 51.69 63.22 67.53 57.31 57.86 NA
Wetting time and water absorption ratio of Erythromycin tablet
0
10
20
30
40
50
ETM-Tab ETME- Tab ETMB- Tab ETMS- Tab ETMN- Tab ETM(m)- Tab
Wetting Time(min) Water Absorption Ratio ( R )
Figure: 11.9. Wetting time and water absorption ratio of tablets prepared from
ETM and their recrystallized agglomerates.
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 325
Dissolution profile of Erythromycin tablet
0
20
40
60
80
100
0 10 20 30 40 50 60
Time(min.)
%C
DR
ETM-Tab ETME-Tab ETMB-Tab
ETMS-Tab ETMN-Tab ETM(m)-Tab
Figure: 11.10. Comparative dissolution studies of prepared erythromycin tablet
with optimized recrystallized agglomerates and marketed tablet.
Figure: 11.11.Shape of macrolide antibiotics tablets prepared from
recrystallized agglomerates.
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 326
11.8. Discussion and Conclusion:
In the field of pharmaceutical powder compaction, it is often necessary to improve the
material flow properties in order to obtain a uniform die-filling in a tablet press. The flow
properties can be enhanced by converting fine powders into larger agglomerates. Wet
granulation is traditionally applied because the equipment and knowledge are available. In
wet granulation, a fluid binder is distributed on a powder blend and subsequently the
granules are dried. A more cost efficient alternative is the dry process—roller compaction
where the material is densified between two counter rotating rolls under pressure forming
a compact ribbon, which is milled into granules. This fairly simple technique is especially
applicable for voluminous materials as it enhances the bulk density greatly. The
disadvantages of the roller compaction comprise the formation of a relative large amount
of dust and fines and the decrease in the compaction properties of powders. Differences in
compression of wet and dry granulated material are observed as wet processed granules
often are more voluminous and roller compacted granules more dense than the original
powder mixture.
There has been renewed interest in examining the potential of direct compression tableting
over recent years in comparison to the use of the more traditional granulation process.
Such manufacture of tablets involves simple mixing and compression of powders, which
results in a number of overall benefits including time and cost savings. Direct compression
tableting is a technique which has been successfully applied to numerous drugs on the
industrial scale, although the success of any procedure, and resulting mechanical
properties of tablets, is strongly affected by the quality of the crystals used. When the
mechanical properties of the drug particles are inadequate a primary granulation is
necessary. The use of spherical crystallization as a technique appears to be an efficient
alternative for obtaining suitable particles for direct tableting. Spherical crystallization is a
particle design technique, by which crystallization and agglomeration can be carried out
simultaneously in one step and which has been successfully utilized for improvement of
flowability and compactibility of crystalline drugs. This technique is also improving the
wettability and dissolution rate of different drug substances.
Blend of all formulations of recrystallized agglomerates except raw macrolide antibiotics
were individually compressed, with out any problem, by direct compression method. A
typical tablet formulation consists of the active Pharmaceutical ingredient(s), fillers,
disintegrants, lubricant and other inactive ingredients. When formulating direct
compression tablets, the choice of binder or diluents is extremely critical since a slight
variation in the binder ratio can lead to capping, lamination, chipping and friable tablets
and all of these are common defects experienced with direct compressible formulations.
Here, microcrystalline cellulose (Avicel PH 102) was used as filler or diluent which
showed excellent compressibility with the recrystallized agglomerates of macrolide
antibiotics. It is self-lubricating (23) and adds compactibility and strength into the tablets
considerably (24). Since the macrolide antibiotic does not possess excellent fluidity and
flow so magnesium stearate was selected as lubricant, because of it, a uniform flow from
hopper to die was possible. It prevents the adhesion of tablet material to the machine parts
such as punches and dies, reduce inter particle friction and facilitates the ejection of tablets
from the die cavity (25).It is hydrophobic and may retard the dissolution of a drug from a
solid dosage form; the lowest possible concentration is therefore used in such formulations
(26-28).
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 327
Table: 11.6, 11.11, 11.16 and 11.21 represents the formulation of tablets by using
recrystallized agglomerates of ATM, CTM, RTM and ETM respectively.
11.8.1. Weight variation and content uniformity:
In order to achieve uniformity in tablet weight, the feed crystals must flow and pack
smoothly into the die cavity of the tablet machine. Therefore, it is essential to improve the
flow and packing properties of the lubricated powder blend. Table 11.7, 11.12, 11.17 and
11.22 represented the flowability parameters in terms of the angle of repose and Carr's
index for lubricated blend of macrolide antibiotics and recrystallized agglomerates. The
data reveals that the lubricated blend with recrystallized agglomerates was much improved
compared to those of lubricated blend containing original raw powders of macrolide
antibiotics. This is due to the large and spherical shape of treated samples obtained in this
study. Fine particles having high surface to mass ratios are more cohesive than coarser
particles, hence more influenced by gravitational force. In addition, powders with similar
particle sizes but dissimilar shapes can have markedly different flow properties owing to
differences in interparticle contact areas. It is generally believed that the flowability of
powders decreases as the shapes of particles become more irregular. These are the main
reasons for an improvement in the flowability of the recrystallized agglomerated powders.
During the compressing of the lubricated blend of tablets with raw crystals of macrolide
antibiotics great friction was indicated by a powerful machine sound. The die cavity was
filled unevenly due to the unfavorable habit of the crystals (irregular stone shaped crystals
shown in SEM study) and their electrostatic charges. In consequence of this a high degree
of pressure force variation could be observed, which also influenced the other parameters,
thus, e.g., deviation from the theoretical mass was high and weight variation exceeded
5%.The lubricated blend of tablets with recrystallized agglomerates of macrolide
antibiotics has a greater particle size and partially spherical, exhibited better properties of
compressibility. Table: 11.8, 11.13, 11.18 and 11.23 represent the weight variation study
of azithromycin, clarithromycin, roxithromycin and erythromycin tablet. The machine
sound caused by friction became less intense and the weight variation value of the tablet
was below 5%, which is related to the great cohesivity value of the recrystallized
agglomerates. The latter can be attributed not only to the shape and size parameters of the
crystals but also to their surface properties. The results obtained with tablets compressed
from the lubricated blend of recrystallized agglomerates were in harmony with the values
of flow property, compactibility and cohesivity of the sample. The crystal agglomerates
can be compressed to tablets almost in a frictionless manner. This was confirmed by the
slight variation of the average weight and weight variation value.
Table: 11.09, 11.14, 11.21 and 11.24 represent the data of content uniformity study of
azithromycin, clarithromycin, roxithromycin and erythromycin tablets. From the obtained
data it reveals that the obtained standard deviation from tablets of macrolide antibiotics
were on significantly higher side compared to tablets prepared from recrystallized
agglomerates. The erratic content uniformity of the tablets prepared from macrolide
antibiotics may be due to irregular particle size and poor flow property.
Table: 11.10, 11.15, 11.20 and 11.25 represent the tablet evaluation data of azithromycin,
clarithromycin, roxithromycin and erythromycin tablets.
11.8.2. Disintegration time (DT):
Tablets made from recrystallized agglomerates of macrolide antibiotics in absence of any
disintegrants did not disintegrate even after 5 minutes. Incorporation of sodium starch
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 328
glycolate resulted in a reduction in the disintegration time. The disintegration time
decreased as a function of disintegrant concentration.
Tablets containing agglomerates without sodium starch glycolate were found to have
longer disintegration times than tablets containing recrystallized agglomerates having
intragranular sodium starch glycolate. The sodium starch glycolate swells very quickly
and results in rapid tablet break-up. The mechanism by which this action takes place
involves rapid absorption of water leading to an enormous increase in volume of tablets
result in rapid and uniform disintegration.
11.8.3. Tablet elastic recovery:
The elastic recoveries of the tablets prepared from recrystallized agglomerates were
smaller than that of the tablets prepared from the original drug crystals. Those findings
suggested that the agglomerated crystals were easily fractured, and the new surface of
crystals produced might contribute to promote plastic deformation under compression.
11.8.4. Tensile strength:
The tensile strength of tablets prepared with agglomerated crystals and untreated raw drug
crystals were calculated. The tablet compressed with the agglomerated crystals exhibited
higher tensile strength than that of compressed tablet with raw crystals of macrolide
antibiotics. This was due to greater plastic deformation of the agglomerated crystals
resulting in greater permanent interparticle contact and strong bond force than the tablets
of raw crystals. This could be also due to superior compactibility of recrystallized
agglomerates in comparison with raw crystals. The results showed that the tablets
prepared using the untreated (original) macrolide antibiotics particles were prone to
capping at higher compression pressure. Where as, in contrast any of the agglomerated
crystals were successfully tableted without capping at any of the compression pressures
applied.
Remarkable fragmentation, increased plastic deformation and lowered elastic recovery of
the agglomerated crystals during tabletting process were responsible for improving the
compactibility. Even at higher compression speed with a single punch tabletting machine,
the agglomerated crystals were tableted directly, although the mechanical strength of
resultant tablet tended to decrease, which was within tolerable difference compared with
that of the tablet with granules. The addition of MCC to the formulation enhance the
plastic deformation potential of formulation resulting in a linear compression
force/crushing strength profile without capping tendency leading to tablet with higher
crushing strength value.
The tablets prepared from the untreated raw macrolide antibiotics showed 100% capping
tendency. The data indicate an appreciable improvement in tabletability of the raw
crystalline materials of macrolide antibiotics following the recrystallization and
agglomeration with different polymers and excipients, owing to fragmentation and better
interlocking of the modified drug particles.
11.8.5. Hardness study:
The tablets prepared with the agglomerated crystals were mechanically stronger (higher
hardness) due to the stronger bonding built between the fresh crystals of agglomerates
fractured under the pressure applied.
11.8.6. Friability study:
The friability of the tablets with macrolide antibiotics raw crystals shows on higher side
above one comparative to all tablets prepared from recrystallized agglomerates of
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 329
macrolide antibiotic. The lower friability value of tablets prepared from recrystallized
agglomerates may be due to higher tensile strength and hardness.
11.8.7. Wetting Time (minutes)/Water Absorption Ratio (R):
The wetting times of tablets were measured and values are tabulated in table. Wetting time
was on higher side and Water Absorption Ratio (R) was on lower side for tablet
containing plain macrolide antibiotics crystals comparative to tablet containing
recrystallized agglomerates of macrolide antibiotics. The tablet containing both intra and
extra granular superdisintegrants show significant changes in both parameters comparative
to other tablets. The good disintegrating property of product was closely related to the
excellent wetting nature of ingredients.
11.8.8. Dissolution study: Tables 11.10, 11.15, 11.20, 11.25 and figures 11.4, 11.6, 11.8, 11.10 represent the in vitro
release data of azithromycin, clarithromycin, roxithromycin and erythromycin tablets
respectively.
The in vitro release of macrolide antibiotics from the tablets containing raw crystals of
macrolide antibiotics is on lower side comparative to the tablets containing recrystallized
agglomerates of macrolide and marketed tablet. For azithromycin tablet, the tablet
containing raw crystals of azithromycin shows 82% release within 60 minutes
comparative to tablet containing its recrystallized agglomerates around 94-97% and
marketed tablet 94%.For clarithromycin tablet, the tablet containing raw crystals of
clarithromycin shows 70% release within 60 minutes comparative to tablet containing its
recrystallized agglomerates around 93-96% and marketed tablet 87%.For roxithromycin
tablet, the tablet containing raw crystals of roxithromycin shows 74% release within 60
minutes comparative to tablet containing its recrystallized agglomerates around 92-96%
and marketed tablet 90%.For erythromycin tablet, the tablet containing raw crystals of
erythromycin shows 74% release within 60 minutes comparative to tablet containing
recrystallized agglomerates around 90-96% and marketed tablet 92%.
As far as the dissolution profile is concerned the similarity factor was calculated by
comparing the dissolution profile data of tablets containing the recrystallized agglomerates
with tablets containing the raw crystals of macrolide antibiotics and marketed tablets. The
similarity factor of tablets dissolution profile containing recrystallized agglomerates of
macrolide antibiotics were below 50 compared with the tablet containing raw crystals of
macrolide antibiotic indicating that tablets with recrystallized agglomerates shows
dissimilar dissolution profile due to change in crystal habit and crystalline form of
recrystallized agglomerates in tablet dosage form. The similarity factor of tablets
dissolution profile containing recrystallized agglomerates of macrolide antibiotics were
above 50 compared with the marketed tablet indicating similar dissolution profile with
marketed tablet.
The cost of the recently used macrolide antibiotics like azithromycin and clarithromycin
was around 11250 and 12500 rupees per kilogram. According to the cost of these
macrolide antibiotics, single 500mg tablet of azithromycin and clarithromycin required
API having cost 5.625 and 6.250 rupees respectively. But the marketed tablets of
azithromycin (Zathrin) and clarithromycin (Claribid) taken for the comparative study
study were around cost 20 and 90 rupees per tablet for azithromycin and clarithromycin
respectively. This difference between the costs is due to the higher manufacturing cost of
marketed tablets. By using the spherical crystallization technique bypassing the
Chapter 11: Preparation and evaluation of tablets from MA and optimized
agglomerates.
Direct tabletting and BA improvement of MA by spherical crystallization tech. 330
granulation process and reduction in the manufacturing cost is possible by reducing the
number of steps involved in the manufacturing process of tablets. The prepared
recrystallized agglomerates are spherical, free flowing and have good compressibility
suitable for direct compression with small quantity of directly compressible excipients into
tablet dosage form. Finally it may be concluded that the prepared recrystallized
agglomerated crystals of MA can be easily formulated into tablet dosage form with
improvement in DT, hardness, friability, tensile strength, wetting time and dissolution rate
as compared to tablets prepared from raw crystals of MA.
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