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INTERNATIONAL JOURNAL OF<br />

RESEARCH ARTICLE<br />

PHARMACEUTICAL INNOVATIONS ISSN 2249-1031<br />

<strong>Formulation</strong> <strong><strong>an</strong>d</strong> <strong>Evaluation</strong> <strong>of</strong> <strong>Orodispersible</strong> <strong>Tablet</strong> <strong>with</strong> <strong>an</strong><br />

Extended Release Pr<strong>of</strong>ile<br />

Chav<strong>an</strong> Ritesh A.* <strong><strong>an</strong>d</strong> Mayee Rahul<br />

Shri Jagdish Prasad Jhabarmal Tibrewala University, Jhunjhunu, Rajasth<strong>an</strong> – 333001<br />

ABSTRACT<br />

Gal<strong>an</strong>tamine is a tertiary alkaloid, selective, competitive <strong><strong>an</strong>d</strong> reversible inhibitor <strong>of</strong> acetyl<br />

cholinesterase. It is used for symptomatic treatment <strong>of</strong> mild to moderately severe dementia <strong>of</strong><br />

the Alzheimer type. Current study was focused on formulation development <strong>of</strong> orodispersible<br />

tablet <strong>of</strong> Gal<strong>an</strong>tamine which disintegrates extended release pellets. Drug coating <strong>of</strong> drug was<br />

done on Celphere CP 203 <strong>with</strong> the help <strong>of</strong> Povidone K30 as a binder. Extended release pellets<br />

were formulated using wurster process. Extended release coating on drug loaded pellets were<br />

done using eudragit NE 30D as a rate limiting polymer. About 30 % extended release coating<br />

<strong>with</strong> eudragit NE 30D showed comparable drug release pattern that <strong>of</strong> <strong>with</strong> marketed<br />

preparation’s pellets <strong>of</strong> Gal<strong>an</strong>tamine ER. Further these pellets were compressed tablets that<br />

were dispersed <strong>with</strong>in 30 seconds, releasing extended release pellets. These formulations<br />

showed ideal drug release comparable to precompressed pellets. It showed no rupture <strong>of</strong><br />

extended release pellets that c<strong>an</strong> hamper the drug release pattern. At accelerated stability<br />

conditions developed formulations were found to be stable for six month.<br />

Keywords – Gal<strong>an</strong>tamine, Extended release orodispersible tablet, extended release pellets,<br />

Eudragit NE 30D, Antialzhimer drug etc.<br />

INTRODUCTION<br />

Orally disintegrating (dissolving) tablets<br />

(ODTs) are solid dosage forms that are<br />

placed in the mouth, rapidly<br />

disintegrate/dissolve when in contact <strong>with</strong><br />

the saliva <strong><strong>an</strong>d</strong> then easily swallowed<br />

<strong>with</strong>out the need for water. The fast<br />

disintegrating behavior <strong>of</strong> the ODT in the<br />

mouth limits the active ingredients that c<strong>an</strong><br />

be incorporated to drugs that exhibit good<br />

taste, stability in gastric conditions <strong><strong>an</strong>d</strong><br />

have long half-life. 1 Bitter tasting drugs<br />

c<strong>an</strong> cause discomfort to patients <strong><strong>an</strong>d</strong><br />

consequently reduce their compli<strong>an</strong>ce,<br />

Volume 3, Issue 3, May − June 2013<br />

whereas incorporating drugs that suffer<br />

from instability in gastric fluids reduces<br />

the efficacy <strong>of</strong> the dosage form<br />

(bioavailability). On the other h<strong><strong>an</strong>d</strong>,<br />

delivering active drugs that have short<br />

half-life in ODTs compromise the<br />

practicality <strong>of</strong> the dosage form as more<br />

frequent administration is required. To<br />

address these issues, a great deal <strong>of</strong> interest<br />

has been directed towards incorporating<br />

multiparticulate drug delivery system in<br />

*Corresponding Author<br />

Chav<strong>an</strong> Ritesh A<br />

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INTERNATIONAL JOURNAL OF<br />

RESEARCH ARTICLE<br />

PHARMACEUTICAL INNOVATIONS ISSN 2249-1031<br />

ODT formulations. The multiparticulate<br />

drug delivery system comprises <strong>of</strong> drug<br />

particles encapsulated or coated by one or<br />

more layers <strong>of</strong> polymers that control the<br />

release <strong>of</strong> the drug. The polymer c<strong>an</strong> be<br />

selected to provide extended, delayed or<br />

pulsed drug delivery, allowing the rate <strong>of</strong><br />

release <strong>of</strong> the drug to be tailored as<br />

required. Moreover, they provide m<strong>an</strong>y<br />

adv<strong>an</strong>tages over single-unit dosage forms<br />

because <strong>of</strong> their multiplicity <strong><strong>an</strong>d</strong> small<br />

sizes including reduced risk <strong>of</strong> systemic<br />

toxicity, enh<strong>an</strong>ced bioavailability, reduced<br />

risk <strong>of</strong> local irritation <strong><strong>an</strong>d</strong> reduced patient<br />

to patient variability as a result <strong>of</strong> their<br />

more predictable gastric emptying.<br />

Accordingly, the formulation <strong>of</strong><br />

multiparticulate into ODTs c<strong>an</strong> extend<br />

their application to more challenging drugs<br />

(e.g. acid sensitive) by overcoming<br />

restrictions imposed by the nature <strong>of</strong> these<br />

drugs <strong><strong>an</strong>d</strong> combine the benefits <strong>of</strong> ODTs<br />

<strong><strong>an</strong>d</strong> multiparticulate drug delivery system 2,<br />

3 . The compression <strong>of</strong> multiparticulate into<br />

ODT formulations has attracted subst<strong>an</strong>tial<br />

attention in both academia <strong><strong>an</strong>d</strong> industry<br />

<strong><strong>an</strong>d</strong> resulted in m<strong>an</strong>y scientific<br />

publications <strong><strong>an</strong>d</strong> patent applications.<br />

However, to produce a tablet <strong>with</strong> good<br />

structural integrity, relatively high<br />

compression pressures are required. These<br />

high pressures c<strong>an</strong> cause damage to the<br />

polymer layers <strong>of</strong> the multiparticulate<br />

system, <strong><strong>an</strong>d</strong>, as a result, compromise their<br />

release controlling properties. Peroral<br />

controlled-release multiple unit dosage<br />

forms (e.g., pellets, gr<strong>an</strong>ules or sustained<br />

release pellets, microcapsules,<br />

microparticles) are becoming more <strong><strong>an</strong>d</strong><br />

more import<strong>an</strong>t on the pharmaceutical<br />

market, as they provide several adv<strong>an</strong>tages<br />

Volume 3, Issue 3, May − June 2013<br />

compared to single-unit dosage forms<br />

(e.g., tablets or capsules) 4,5<br />

Gal<strong>an</strong>tamine is a tertiary alkaloid,<br />

selective, competitive <strong><strong>an</strong>d</strong> reversible<br />

inhibitor <strong>of</strong> acetyl cholinesterase. It is used<br />

for symptomatic treatment <strong>of</strong> mild to<br />

moderately severe dementia <strong>of</strong> the<br />

Alzheimer type. Currently available<br />

formulations for gal<strong>an</strong>tamine are in the<br />

form <strong>of</strong> pellets, capsules for extended<br />

release <strong><strong>an</strong>d</strong> conventional tablets for<br />

immediate release 6 . By looking at target<br />

population for Gal<strong>an</strong>tamine, orodispersible<br />

tablet <strong>with</strong> extended release pr<strong>of</strong>ile could<br />

be favorable option that could administer<br />

the dosage form easily. The present work<br />

led to the formulation <strong>of</strong> orodispersible<br />

tablets for oral administration. The<br />

developed formulation which disintegrates<br />

disperses in oral cavity in less th<strong>an</strong> 30<br />

seconds <strong>with</strong>out the need <strong>of</strong> drinking<br />

water; had pleas<strong>an</strong>t mouth feel <strong><strong>an</strong>d</strong><br />

improved patient compli<strong>an</strong>ce particularly<br />

for those who have difficulty in<br />

swallowing 7 .<br />

MATERIALS AND METHODS<br />

Materials<br />

Gal<strong>an</strong>tamine Hydrobromide was selected<br />

as a model drug c<strong><strong>an</strong>d</strong>idate for the<br />

formulation trials aqueous dispersion <strong>of</strong><br />

Eudragit NE 30D was used as a rate<br />

controlling polymer. Talc was used as <strong>an</strong><br />

<strong>an</strong>titacking agent. Celphere CP 203 pellets<br />

from Asahi Kasei Excipients were used as<br />

a core pellets for drug loading. Water <strong><strong>an</strong>d</strong><br />

Meth<strong>an</strong>ol (GR grade) was used as<br />

solvents. Microcrystalline cellulose <strong>of</strong><br />

various grades viz. Ceolus KG 802 <strong><strong>an</strong>d</strong><br />

KG 1000 (Bl<strong>an</strong>ver) were used as a filler<br />

which provides good cushioning effect to<br />

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PHARMACEUTICAL INNOVATIONS ISSN 2249-1031<br />

the pellets. Crosspovidone XL 10 (ISP<br />

chemicals) was used as a disintegr<strong>an</strong>t.<br />

Glyceryl Stearate was used a waxy agent<br />

to promote easy flow <strong>of</strong> pellets. Flavour<br />

(firmenich) was used as a flavour.<br />

Aspartame as a sweetener. Magnesium<br />

Stearate was used as a lubric<strong>an</strong>t.<br />

METHODS<br />

<strong>Formulation</strong> Development<br />

Drug loading<br />

Procedure:-<br />

Refer the table no. 1 for the formula.<br />

Gal<strong>an</strong>tamine Hydrobromide was dissolved<br />

in purified water under continuous stirring<br />

until it gets completely dissolved then<br />

Povidone K30 was added slowly under<br />

continuous stirring in vertex. Stirring was<br />

continued until clear solution obtained.<br />

Finally above drug loading solution so<br />

formed was then subjected for drug<br />

loading over Celphere CP 203 pellets in<br />

Fluidized Bed Equipment (Pam Glatt) <strong>with</strong><br />

bottom spray attachment <strong>of</strong> 1.0 mm spray<br />

gun having fixed column height. After<br />

drug loading, drug loaded pellets were<br />

then dried at 50 0 C until LOD achieved<br />

NMT 1.5 % w/w. <strong><strong>an</strong>d</strong> then sifted through<br />

ASTM mesh # 60.<br />

Process parameters were set as in table<br />

no.2.<br />

Extended Release Coating<br />

Procedure:-<br />

Refer the table no. 3 for the formula .Talc<br />

was dispersed in purified water under<br />

continuous stirring for 30 min, then<br />

Eudragit NE 30 D was added under<br />

continuous stirring <strong><strong>an</strong>d</strong> Stirred for <strong>an</strong>other<br />

30 minutes more. Finally above extended<br />

release coating solution was then subjected<br />

for enteric coating over drug loaded pellets<br />

Volume 3, Issue 3, May − June 2013<br />

<strong>of</strong> Gal<strong>an</strong>tamine in Fluidized Bed<br />

Equipment (Pam Glatt) <strong>with</strong> bottom spray<br />

attachment <strong>of</strong> 1.0 mm spray gun having<br />

fixed column height. During the process<br />

samples <strong>of</strong> extended release coated pellets<br />

each at 10, 20, 30, 40 <strong><strong>an</strong>d</strong> 50 % extended<br />

release coating, was removed periodically<br />

<strong><strong>an</strong>d</strong> subjected for curing in oven at 50 0 c for<br />

1 hr. Withdrawn samples were then passed<br />

through ASTM mesh #30 <strong><strong>an</strong>d</strong> 50 <strong><strong>an</strong>d</strong><br />

retained pellets on ASTM mesh # 50 were<br />

subjected for dissolution <strong><strong>an</strong>d</strong> subsequently<br />

for further study. Process parameters were<br />

set as in table no.4.<br />

From the in vitro drug release patterns <strong><strong>an</strong>d</strong><br />

curing effects <strong>of</strong> extended release pellets<br />

<strong>of</strong> appropriate coating that matches to in<br />

vitro drug release pr<strong>of</strong>ile <strong>of</strong> marketed<br />

preparation, were selected for further<br />

evaluation <strong><strong>an</strong>d</strong> subsequently compression<br />

process.<br />

Compression <strong>of</strong> Pellets<br />

Procedure<br />

Refer the table no. 5 for the formula<br />

.Ceolus KG 1000 <strong><strong>an</strong>d</strong> 802, Crospovidone<br />

XL 10, Aspartame <strong><strong>an</strong>d</strong> flavor were passed<br />

through mesh # 30 separately. Magnesium<br />

Stearate was passed through mesh # 60.All<br />

ingredients except magnesium Stearate<br />

was blended <strong>with</strong> extended release pellets<br />

were blended in polybag for 5 minutes.<br />

Magnesium Stearate was then lubricated<br />

<strong>with</strong> the above blend for 2 minutes <strong><strong>an</strong>d</strong><br />

subjected for compression <strong>with</strong> 13 mm<br />

biconvex round shaped punch.Compressed<br />

tablets were evaluated for Appear<strong>an</strong>ce <strong><strong>an</strong>d</strong><br />

dimensions, Thickness, Hardness,<br />

Friability, Disintegration, in vitro drug<br />

release <strong><strong>an</strong>d</strong> stability studies 8, 9 .<br />

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RESEARCH ARTICLE<br />

PHARMACEUTICAL INNOVATIONS ISSN 2249-1031<br />

<strong>Evaluation</strong> <strong>of</strong> Lubricated Blend <strong><strong>an</strong>d</strong><br />

Pellets<br />

Angle <strong>of</strong> repose<br />

The powder mixture was allowed to pass<br />

through the funnel fixed to a st<strong><strong>an</strong>d</strong> at<br />

definite height. The <strong>an</strong>gle <strong>of</strong> repose was<br />

then calculated by measuring the height<br />

<strong><strong>an</strong>d</strong> radius <strong>of</strong> the heap <strong>of</strong> powder formed.<br />

Then <strong>an</strong>gle <strong>of</strong> repose had been calculated<br />

from below formula<br />

θ = t<strong>an</strong> -1 (h/r)<br />

Where:<br />

θ = Angle <strong>of</strong> repose<br />

h = Height <strong>of</strong> pile in cm<br />

r = radius in cm.<br />

Bulk Density<br />

Accurately weighed qu<strong>an</strong>tity <strong>of</strong> sample,<br />

<strong><strong>an</strong>d</strong> carefully poured into graduated<br />

cylinder. Then after pouring the powder<br />

into the graduated cylinder the powder bed<br />

was made uniform <strong>with</strong>out disturbing.<br />

Then the volume was measured directly<br />

from the graduation marks on the cylinder<br />

as ml. The volume measure was called as<br />

the bulk volume <strong><strong>an</strong>d</strong> the bulk density is<br />

calculated by following formula:<br />

Bulk density = Weight <strong>of</strong> powder /Bulk<br />

volume<br />

Tapped Density<br />

After measuring the bulk volume the same<br />

measuring cylinder was set into tap density<br />

apparatus. The tap density apparatus was<br />

set to 100 taps drop <strong><strong>an</strong>d</strong> operated for 50<br />

taps. Volume was noted as (Va) <strong><strong>an</strong>d</strong> again<br />

tapped for 50 times <strong><strong>an</strong>d</strong> volume was noted<br />

as (Vb). If the difference between Va <strong><strong>an</strong>d</strong><br />

Vb not greater th<strong>an</strong> 2% then Vb is consider<br />

as final tapped volume. The tapped density<br />

is calculated by the following Formula:<br />

Tapped Density = Va / Vb<br />

Where<br />

Va = weight <strong>of</strong> the powder<br />

Vb = tapped volume <strong>of</strong> the packing<br />

Compressibility index <strong><strong>an</strong>d</strong> Hausner<br />

ratio:-<br />

Compressibility index <strong><strong>an</strong>d</strong> Hausner ratio<br />

were calculated from bulk <strong><strong>an</strong>d</strong> tapped<br />

density <strong>of</strong> the sample. These parameters<br />

show the flow properties <strong>of</strong> sample.<br />

Compressibility index = [(D T - D B )/ D T ] x<br />

100<br />

Hausner ratio = D T / D B<br />

D T =Tapped density<br />

D B = Bulk density<br />

Friability test<br />

Roche Friabilator was used to measure the<br />

friability <strong>of</strong> the pellets. It was rotated at a<br />

rate <strong>of</strong> 25 RPM. 5 g pellets were weighed<br />

collectively <strong><strong>an</strong>d</strong> placed in the chamber <strong>of</strong><br />

the friabilator. After 100 rotations (4<br />

minutes), the pellets were taken out from<br />

the friabilator <strong><strong>an</strong>d</strong> intact pellets were again<br />

weighed collectively after removing fines<br />

using ASTM sieve # 60 sieve. Permitted<br />

percentage friability limit is 0.8%. The<br />

percent friability was determined using the<br />

following formula.<br />

% friability = [(W 1 – W 2 ) / W 1 ] x 100<br />

Where<br />

W 1 = weight <strong>of</strong> the pellets before test.<br />

W 2 = weight <strong>of</strong> the pellets after test.<br />

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PHARMACEUTICAL INNOVATIONS ISSN 2249-1031<br />

Drug content (Assay calculation)<br />

This practice was done for the pellets<br />

obtained after drug coating to check the<br />

entrapment <strong>of</strong> the drug in the drug loaded<br />

pellets. Drug loaded pellets equivalent to<br />

24 mg <strong>of</strong> pellets had been dissolved in<br />

diluents, from this solution 1ml was<br />

pipette out in to 10ml volumetric flask <strong><strong>an</strong>d</strong><br />

volume was made up to <strong>with</strong> meth<strong>an</strong>ol 10 .<br />

In vitro drug release<br />

In vitro drug release <strong>of</strong> pellets was carried<br />

out after functional coating to check drug<br />

release pattern <strong>of</strong> the extended release<br />

pellets prior to the compression <strong><strong>an</strong>d</strong> on to<br />

the compressed tablets. Invitro drug<br />

release/ dissolution studies were carried<br />

out using following dissolution conditions.<br />

Dissolution Conditions:-<br />

Dissolution Apparatus = USP type<br />

II (Paddle type).<br />

Dissolution medium = Phosphate<br />

buffer pH 6.8<br />

Temperature = 37 ± 0.5 o C<br />

Paddle rpm = 100.<br />

Time Points =<br />

1,2,3,4,6,8,10,12,14,16,18,20,22,24<br />

hrs.<br />

Accurately weighed pellets were placed in<br />

each flask <strong>of</strong> dissolution apparatus. The<br />

apparatus was allowed to run for 24 hours.<br />

Samples measuring 5 ml were <strong>with</strong>drawn.<br />

Then samples were filtered through 0.45<br />

Millipore filter <strong><strong>an</strong>d</strong> their concentrations<br />

were determined using High Perform<strong>an</strong>ce<br />

Liquid Chromatography System 11<br />

Curing effect:<br />

The pellets were cured in a hot air oven for<br />

24 hours to check the effect <strong>of</strong> curing on<br />

drug release; the cured pellets are<br />

subjected for in vitro release studies 12 .<br />

Volume 3, Issue 3, May − June 2013<br />

EVALUATION OF COMPRESSED<br />

TABLETS:-<br />

Appear<strong>an</strong>ce <strong><strong>an</strong>d</strong> Dimensions:-<br />

The thickness <strong><strong>an</strong>d</strong> diameter <strong>of</strong> the tablets<br />

was determined using a Vernier calliper.<br />

Five tablets from each type <strong>of</strong> formulation<br />

were used <strong><strong>an</strong>d</strong> average values were<br />

calculated. It is expressed in mm.<br />

Weight variation test:-<br />

Twenty tablets were selected r<strong><strong>an</strong>d</strong>omly<br />

from each formulation, weighed<br />

individually <strong><strong>an</strong>d</strong> the average weight <strong><strong>an</strong>d</strong> %<br />

variation <strong>of</strong> weight was calculated.<br />

Hardness<br />

For each formulation, the hardness <strong>of</strong> 3<br />

tablets was determined using the Mons<strong>an</strong>to<br />

hardness tester. The tablet was held along<br />

its oblong axis in between the two jaws <strong>of</strong><br />

the tester. Then const<strong>an</strong>t force was applied<br />

by rotating the knob until the tablet<br />

fractured. The value at this point was<br />

noted.<br />

Friability<br />

For each formulation, the friability <strong>of</strong> 20<br />

tablets was determined using the Roche<br />

friabilator. A sample <strong>of</strong> preweighed 20<br />

tablets was placed in Roche friabilator,<br />

which was then operated for 25 RPM for 4<br />

minutes. A loss <strong>of</strong> less th<strong>an</strong> 1% in weigh in<br />

generally considered acceptable. Percent<br />

friability (% F) was calculated as follows,<br />

% friability = [(W 1 – W 2 ) / W 1 ] x 100<br />

Whereas W 1 = weight <strong>of</strong> tablets before<br />

test.<br />

W 2 = weight <strong>of</strong> the tablets after test.<br />

In vitro disintegration test<br />

The process <strong>of</strong> breakdown <strong>of</strong> a tablet into<br />

smaller particles is called as disintegration.<br />

The in-vitro disintegration time <strong>of</strong> a tablet<br />

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was determined using disintegration<br />

apparatus as per USP specifications.<br />

In vitro drug release<br />

Same as in vitro drug release testing <strong>of</strong><br />

pellets.<br />

Stability Studies<br />

Stability studies were conducted according<br />

to ICH guidelines by using optimized<br />

formulation at 40°C/75±5% RH or a<br />

period <strong>of</strong> 6 months. The samples were<br />

<strong>with</strong>drawn at 1, 3 <strong><strong>an</strong>d</strong> 6 month <strong><strong>an</strong>d</strong><br />

<strong>an</strong>alyzed for drug content, <strong><strong>an</strong>d</strong> dissolution<br />

study as given in in-vitro release<br />

dissolution studies by <strong>an</strong> HPLC method.<br />

Drug content (Assay calculation)<br />

Twenty tablets were weighed <strong><strong>an</strong>d</strong><br />

powdered. The blend equivalent to 24 mg<br />

<strong>of</strong> Gal<strong>an</strong>tamine was weighed <strong><strong>an</strong>d</strong><br />

dissolved in sufficient qu<strong>an</strong>tity <strong>of</strong> PH 6.8<br />

phosphate buffer. The solution was filtered<br />

through Whatm<strong>an</strong>n filter paper (no.41),<br />

suitably diluted <strong>with</strong> pH 6.8 phosphate<br />

buffer <strong><strong>an</strong>d</strong> assayed.<br />

RESULT AND DISCUSSION<br />

Drug loading<br />

Drug solution <strong>of</strong> Gal<strong>an</strong>tamine hydro<br />

bromide was loaded on Celphere CP 203<br />

pellets Due to low viscous solution drug<br />

loading process was done <strong>with</strong>out <strong>an</strong>y<br />

process issues. Further drug loaded pellets<br />

were evaluated.<br />

Moisture Content<br />

Loss on drying was measured using<br />

moisture <strong>an</strong>alyzer at 105 0 c <strong><strong>an</strong>d</strong> was found<br />

to be 1.13 %w/w.<br />

Assay content<br />

130 mg <strong>of</strong> drug loaded Pellets equivalent<br />

to 24 mg <strong>of</strong> Gal<strong>an</strong>tamine was subjected for<br />

assay determination by HPLC which was<br />

Volume 3, Issue 3, May − June 2013<br />

found to be 98.93 % which shows effective<br />

drug loading on inert pellets.<br />

Friability<br />

Friability <strong>of</strong> drug loaded pellets was found<br />

to be 0.361 which showed enough strength<br />

to <strong>with</strong>st<strong><strong>an</strong>d</strong> <strong>an</strong>y pellets breaking issues<br />

during pelletisation.<br />

EXTENDED RELEASE COATING<br />

Extended release coating was done on drug<br />

loaded pellets. Due to low glass tr<strong>an</strong>sition<br />

temperature <strong>of</strong> eudragit NE 30D, process<br />

was done using slow rate <strong>of</strong> spray rate.<br />

Also it was found that increasing spray<br />

rate triggers the sticking <strong>of</strong> pellets which<br />

was not ideal condition for rate controlling<br />

issue. Parameters observed during<br />

extended release coating were as below.<br />

Samples were <strong>with</strong>drawn at different<br />

coating levels <strong><strong>an</strong>d</strong> then subjected for<br />

curing at 50 0 c for 1 hr. Cured pellets were<br />

then passed through ASTM mesh # 30 <strong><strong>an</strong>d</strong><br />

50. Pellets retained on ASTM mesh #50<br />

was subjected for dissolution to check<br />

drug release pattern <strong>of</strong> the extended release<br />

pellets <strong><strong>an</strong>d</strong> drug release was found to be<br />

as in table no. 6 <strong><strong>an</strong>d</strong> graph no.1.<br />

It was found that coated 30% extended<br />

release coated pellets were found to be<br />

comparable <strong>with</strong> marketed extended<br />

release pellets. So these were chosen for<br />

further studies as below.<br />

Moisture Content:-<br />

Loss on drying was measured using<br />

moisture <strong>an</strong>alyzer at 105 0 c <strong><strong>an</strong>d</strong> was found<br />

to be 0.89 %w/w.<br />

Friability<br />

Friability <strong>of</strong> extended release pellets was<br />

found to be 0.453 at 300 RPM which<br />

showed enough strength to <strong>with</strong>st<strong><strong>an</strong>d</strong> <strong>an</strong>y<br />

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pellets breaking issues during<br />

compression.<br />

Effect <strong>of</strong> Curing on extended release<br />

pellets.<br />

The pellets were cured in a hot air oven for<br />

24 hours at 60 o c to check the effect <strong>of</strong><br />

curing on drug release. Periodically pellets<br />

were sampled <strong><strong>an</strong>d</strong> then subjected for in<br />

vitro drug release studies <strong><strong>an</strong>d</strong> compared<br />

<strong>with</strong> previous initial results. It had been<br />

found that there is no drastic effect on drug<br />

release after curing for long time. This<br />

shows the promising stability <strong>of</strong> extended<br />

release coating. In vitro drug release was<br />

found to be as in table no.7 <strong><strong>an</strong>d</strong> graph<br />

no.2.<br />

Further Extended release pellets were<br />

evaluated for precompression parameters<br />

as Angle <strong>of</strong> Repose, Bulk density, Tapped<br />

density, Compressibility index, Hausner<br />

ratio as below which showed good flow<br />

property as statedin table no.8.<br />

Further these pellets were subjected for<br />

blending <strong><strong>an</strong>d</strong> lubrication <strong>with</strong><br />

extragr<strong>an</strong>ular ingredients<br />

Compression<br />

Lubricated blend was then subjected for<br />

preformulation studies to check flowability<br />

<strong><strong>an</strong>d</strong> compressibility properties as stated in<br />

table no. 10. Then lubricated blend was<br />

compressed into tablets by using 13.0 mm<br />

biconvex round shaped punch. In process<br />

compression parameters as followed in<br />

table no. 11.<br />

Since disintegration was achieved on the<br />

above parameters hence tablets were<br />

compressed <strong><strong>an</strong>d</strong> subjected for dissolution<br />

to check that if there was <strong>an</strong>y ch<strong>an</strong>ce <strong>of</strong><br />

rupturing extended release pellets during<br />

the compression, as in table no. 12.<br />

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It had been observed that there was no<br />

impact on dissolution pr<strong>of</strong>ile <strong>of</strong><br />

compressed tablets <strong><strong>an</strong>d</strong> extended release<br />

pellets, also on this hardness there was no<br />

rupture <strong>of</strong> pellets during compression <strong>with</strong><br />

enough tablet friability.<br />

Stability study<br />

Stability studies were conducted according<br />

to ICH guidelines by using optimized<br />

formulation at 40°C/75±5% RH or a<br />

period <strong>of</strong> 6 months. The samples were<br />

<strong>with</strong>drawn at 1,3 <strong><strong>an</strong>d</strong> 6 month <strong><strong>an</strong>d</strong><br />

<strong>an</strong>alyzed for drug content, <strong><strong>an</strong>d</strong> dissolution<br />

study as given in in-vitro release<br />

dissolution studies by <strong>an</strong> HPLC method as<br />

in Table no. 13,14 <strong><strong>an</strong>d</strong> graph no. 4.<br />

REFERENCES<br />

1. Akbari B.V., Dholakiya R.B.,<br />

Shiy<strong>an</strong>i B.G., Lodhiya D.J. Design,<br />

development <strong><strong>an</strong>d</strong> characterization<br />

<strong>of</strong> mouth dissolving tablets <strong>of</strong><br />

cinnarizine using superdisintegr<strong>an</strong>ts.<br />

International journal<br />

<strong>of</strong> pharmtech research . Vol.2,<br />

no.1, pp 97-105 J<strong>an</strong>-Mar 2010<br />

2. Aulton, M.E.,Kh<strong>an</strong>, K.A., The<br />

strength <strong><strong>an</strong>d</strong> compaction <strong>of</strong><br />

millispheres. The design <strong>of</strong> a<br />

controlled-release drug delivery<br />

system for ibupr<strong>of</strong>en in the form <strong>of</strong><br />

a tablet comprising compacted<br />

polymer-coated millispheres. Drug<br />

Dev. Ind. Pharm., 20, 3069-3104,<br />

1994.<br />

3. Bechgaard H., Nielsen G.H.<br />

Controlled-Release Multiple-Units<br />

<strong><strong>an</strong>d</strong> Single-Unit Doses a Literature<br />

Review. Drug Development <strong><strong>an</strong>d</strong><br />

Industrial Pharmacy 4, 53 – 67,<br />

1978.<br />

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4. Bodmeier, R., <strong>Tablet</strong>ing <strong>of</strong> pellets.<br />

Europe<strong>an</strong> Journal <strong>of</strong> Pharmaceutics<br />

<strong><strong>an</strong>d</strong> Biopharmaceutics . 1997.<br />

5. Dashevsky, A., Kolter, K.,<br />

Bodmeier, R., Compression <strong>of</strong><br />

pellets coated <strong>with</strong> various aqueous<br />

polymer dispersions. Int. J. Pharm.<br />

279 (1-2), 19-26. 2004.<br />

6. http://www.drugb<strong>an</strong>k.ca/drugs/DB<br />

00674<br />

7. Joh<strong>an</strong>sson, B., Nicklasson, F.,<br />

Alderborn, G., Effect <strong>of</strong> pellet size<br />

on degree <strong>of</strong> deformation <strong><strong>an</strong>d</strong><br />

densification during compression<br />

<strong><strong>an</strong>d</strong> on compactability <strong>of</strong><br />

microcrystalline cellulose pellets.<br />

Int. J. Pharm., 163, 35-48. 1998.<br />

8. Joh<strong>an</strong>sson, B., Wikberg, M., Ek,<br />

R., Alderborn, G., Compression<br />

behaviour <strong><strong>an</strong>d</strong> compactability <strong>of</strong><br />

microcrystalline cellulose pellets in<br />

relationship to their pore structure<br />

<strong><strong>an</strong>d</strong> mech<strong>an</strong>ical properties. Int. J.<br />

Pharm., 117, 57-73. 1995.<br />

9. Juslin, M., Turakka, L.,<br />

Puumalainen, P., Controlled<br />

release tablets. Part 1: The use <strong>of</strong><br />

pellets coated <strong>with</strong> a retarding<br />

acrylate plastic in tabletting.<br />

Pharm. Ind., 42, 829-832, 1980.<br />

10. Satyakala G<strong>an</strong>ti. Development <strong>of</strong><br />

HPLC Methods For<br />

Pharmaceutically Relev<strong>an</strong>t<br />

Molecules; Method Tr<strong>an</strong>sfer To<br />

UPLC. Comparing Methods<br />

Statistically For Equivalence.<br />

Temple University Graduate<br />

Board. J<strong>an</strong>uary 2011.<br />

11. T. Jagadeesh, R. Bala Ramesha<br />

Chary. Development <strong>of</strong> Oral Multi<br />

Particulate Drug Delivery System<br />

<strong>of</strong> Gal<strong>an</strong>tamine Hydrobromide by<br />

Using Extrusion Spheronization<br />

technique. International Journal <strong>of</strong><br />

Pharmacy & Technology. IJPT |<br />

June-2011 | Vol. 3 | Issue No.2 |<br />

2633-2643<br />

12. Korber, M., V. H<strong>of</strong>fart, et al.<br />

(2010). "Effect <strong>of</strong> unconventional<br />

curing conditions <strong><strong>an</strong>d</strong> storage on<br />

pellets coated <strong>with</strong> Aquacoat<br />

ECD." Drug Development <strong><strong>an</strong>d</strong><br />

Industrial Pharmacy 36(2): 190-<br />

199.<br />

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Table No. 1 Formula for drug loading<br />

Sr. No. Ingredients % w/w<br />

1 Gal<strong>an</strong>tamine Hydrobromide (Eq. to 24 mg <strong>of</strong> Gal<strong>an</strong>tamine) 23.66<br />

2 Polyvinyl Pyrrolidone (Povidone K30) 2.37<br />

3 Celphere CP203 73.97<br />

4 Purified water 107.69<br />

Table No. 2 Set Parameters <strong>of</strong> drug loading.<br />

Parameters<br />

Set value<br />

Inlet temperature ( 0 C) 50<br />

Product temperature ( 0 C) 45<br />

Exhaust temperature ( 0 C) 45<br />

Atomisation Air (bar) 0.8-0.9<br />

F<strong>an</strong> speed 20-50<br />

Peristaltic Pump Speed (RPM) 1-10<br />

Table No. 3 Formula for extended release coating.<br />

Sr. No. Ingredients % w/w<br />

1 Eudragit NE 30 D * 50.00<br />

2 Talc 50.00<br />

3 Purified water q.s.<br />

*Solid content.<br />

Table No. 4 Set Parameters <strong>of</strong> drug loading.<br />

Parameters<br />

Set values<br />

Inlet temperature ( 0 C) 25<br />

Product temperature ( 0 C) 20-25<br />

Exhaust temperature ( 0 C) 20-25<br />

Atomisation Air (bar) 0.9-1.0<br />

F<strong>an</strong> speed 30-75<br />

Peristaltic Pump Speed (RPM) 1-5<br />

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Table No. 5 Formula for blending <strong><strong>an</strong>d</strong> lubrication <strong>of</strong> extended release pellets.<br />

Sr. No. Ingredients % w/w<br />

1 Extended Release Pellets 42.25<br />

2 Ceolus KG 1000* 24.55<br />

3 Ceolus KG 802 18.45<br />

4 Glyceryl Stearate 2.50<br />

5 Crospovidone XL 10 10.00<br />

6 Or<strong>an</strong>ge Flavor 0.50<br />

7 Aspartame 0.50<br />

8 Magnesium Stearate 1.25<br />

<strong>Tablet</strong> weight<br />

400.00 mg<br />

*To be adjusted in accord<strong>an</strong>ce <strong>with</strong> extended release pellets weight<br />

Table- 6 In vitro drug release pr<strong>of</strong>ile <strong>of</strong> extended release pellets at different coating levels.<br />

Time<br />

(Hours)<br />

Marketed<br />

sample<br />

Percentage <strong>of</strong> drug released<br />

10 % 20 % 30 %<br />

ERC ERC ERC<br />

40 %<br />

ERC<br />

50 %<br />

ERC<br />

0 0 0 0 0 0 0<br />

1 28 48 38 26 23 14<br />

2 40 62 51 38 31 20<br />

3 52 72 60 47 39 31<br />

4 60 81 69 57 50 38<br />

6 74 92 83 70 63 52<br />

8 81 99 89 79 73 68<br />

10 85 100 95 84 79 75<br />

12 89 100 96 87 83 79<br />

14 90 99 99 88 86 84<br />

16 92 100 100 91 90 88<br />

18 95 100 99 94 92 89<br />

20 97 99 100 96 93 92<br />

22 99 98 100 98 96 93<br />

24 100 99 99 99 98 95<br />

F2 Value 35.24 50.52 74.40 50.99 36.71<br />

ERC= Extended release coating<br />

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Table-7 In vitro drug release pr<strong>of</strong>ile <strong>of</strong> cured extended release pellets at different time<br />

intervals<br />

Percentage <strong>of</strong> drug released<br />

Time<br />

Cured pellets Cured pellets Cured pellets<br />

(Hours)<br />

(Initial) for 12 hrs. for 24 hrs.<br />

0 0 0 0<br />

1 26 24 23<br />

2 38 36 35<br />

3 47 45 43<br />

4 57 55 54<br />

6 70 68 67<br />

8 79 77 75<br />

10 84 82 81<br />

12 87 85 84<br />

14 88 86 84<br />

16 91 90 88<br />

18 94 92 89<br />

20 96 93 92<br />

22 98 96 94<br />

24 99 98 97<br />

F2 Value 74.40 64.16 59.20<br />

Table No 8 Precompression parameters <strong>of</strong> extended release pellets<br />

Sr. No. Parameters Results Remark<br />

1 Bulk Density 0.720 g/ml<br />

2 Tapped Density 0.810 g/ml<br />

3 Hausners ratio 1.12 Good flow<br />

4 Compressibility index 10.62 % Good flow<br />

5 Angle <strong>of</strong> repose 13.24 o Good flow<br />

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Table No. 9 Formula for blending <strong><strong>an</strong>d</strong> lubrication <strong>of</strong> extended release pellets<br />

Sr. No. Ingredients % w/w<br />

1 Extended Release Pellets 42.25<br />

2 Ceolus KG 1000* 24.55<br />

3 Ceolus KG 802 18.45<br />

4 Glyceryl Stearate 2.50<br />

5 Crospovidone XL 10 10.00<br />

6 Flavor 0.50<br />

7 Aspartame 0.50<br />

8 Magnesium Stearate 1.25<br />

<strong>Tablet</strong> weight 100.00<br />

Table No.10 Preformulation parameters <strong>of</strong> lubricated blend.<br />

Sr. No. Parameters Results Remark<br />

1 Bulk Density 0.660 g/ml<br />

2 Tapped Density 0.760 g/ml<br />

3 Hausners ratio 1.15 Good flow<br />

4 Compressibility index 12.88 % Good flow<br />

5 Angle <strong>of</strong> repose 13.24 o Good flow<br />

Table No. 11 In process compression parameters<br />

Sr. No. Parameters Results Remark<br />

1 Uniformity <strong>of</strong> weight ( mg) 394-205<br />

2 Weight variation 2.25 % deviation<br />

Within Limit<br />

3 Thickness (mm) 2.50±0.16 mm<br />

4 Hardness (kP) 2.9-3.5<br />

5 Friability ( for 100 revolutions) 0.451 Within Limit<br />

6 In-vitro disintegration time (sec) 18-28 Within Limit<br />

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Table No. 12 Comparative dissolution pr<strong>of</strong>ile <strong>of</strong> Extended release pellets <strong><strong>an</strong>d</strong><br />

compressed tablets.<br />

Time (Hours)<br />

Percentage <strong>of</strong> drug released<br />

Extended Release Pellets Compressed tablets<br />

0 0 0<br />

1 26 24<br />

2 38 36<br />

3 47 45<br />

4 57 55<br />

6 70 68<br />

8 79 77<br />

10 84 82<br />

12 87 85<br />

14 88 86<br />

16 91 90<br />

18 94 92<br />

20 96 93<br />

22 98 97<br />

24 99 98<br />

F2 Value 74.40 64.16<br />

Table No. 13 Drug content according to stability conditions.<br />

Sr.No. Stability Conditions Drug content<br />

1 Initial 99.93 %<br />

2 40 o c/75% RH, 1 month. 99.27<br />

3 40 o c/75% RH, 2 month. 98.69<br />

4 40 o c/75% RH, 3 month. 98.21<br />

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% Drug released<br />

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Table No. 14 In vitro drug release pattern <strong>of</strong> stabilised formulations.<br />

Time<br />

(Hours)<br />

Initial<br />

Percentage <strong>of</strong> drug released<br />

40 o C/75% RH,<br />

1 month<br />

40 o C/75% RH<br />

2 month<br />

40 o C/75% RH,<br />

3 month<br />

0 0 0 0 0<br />

1 24 23 21 22<br />

2 36 34 35 33<br />

3 45 44 42 41<br />

4 55 56 55 53<br />

6 68 68 66 65<br />

8 77 75 73 74<br />

10 82 82 81 80<br />

12 85 84 83 82<br />

14 86 84 83 83<br />

16 90 88 86 85<br />

18 92 91 91 89<br />

20 93 93 94 92<br />

22 97 97 95 94<br />

24 98 98 97 98<br />

F2 values 74.40 61.01 56.46 54.42<br />

100<br />

90<br />

80<br />

70<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

Marketed sample<br />

10 % Extended release coating<br />

20 % Extended release coating<br />

30 % Extended release coating<br />

40 % Extended release coating<br />

50 % Extended release coating<br />

0 2 4 6 8 10 12 14 16 18 20 22 24<br />

Time (Hours)<br />

Graph-1 In vitro drug release pr<strong>of</strong>ile <strong>of</strong> extended release pellets at different coating levels<br />

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% Drug released<br />

% Drug released<br />

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100<br />

90<br />

80<br />

70<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

0 2 4 6 8 10 12 14 16 18 20 22 24<br />

Time (Hours)<br />

Cured pellets (Initial)<br />

Cured pellets for 12 hrs.<br />

Cured pellets for 24 hrs.<br />

Graph -2 In vitro drug release pr<strong>of</strong>ile <strong>of</strong> cured extended release pellets at different time intervals<br />

100<br />

90<br />

80<br />

70<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

0 2 4 6 8 10 12 14 16 18 20 22 24<br />

Time (Hours)<br />

Extended Release Pellets<br />

Compressed tablets<br />

Graph - 3 Comparative dissolution pr<strong>of</strong>ile <strong>of</strong> Extended release pellets <strong><strong>an</strong>d</strong> compressed tablets.<br />

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% Drug released<br />

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100<br />

90<br />

80<br />

70<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

0 2 4 6 8 10 12 14 16 18 20 22 24<br />

Time (Hours)<br />

Initial<br />

40oc/75% RH, 1 month.<br />

40oc/75% RH, 3month.<br />

40oc/75% RH, 6 month.<br />

Graph - 4 In vitro drug release data <strong>of</strong> stabilised formulation<br />

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