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www.iajpr.com Page1552 Indo American Journal of Pharmaceutical Research, 2013 ISSN NO: 2231-6876 Journal home page: http://www.iajpr.com/index.php/en/ INDO AMERICAN JOURNAL OF PHARMACEUTICAL RESEARCH FORMULATION AND EVALUATION OF TETRAETHYLTHIURAM DISULPHIDE TABLETS BY AQUEOUS WET GRANULATION PROCESS Venkateswaran Chidambaram Seshadri, Packiaraj Jeyachandran Manohari, Janakiraman Kunchithapatham Department of Pharmacy, Annamalai University, Annamalai Nagar, Chidambaram, Pin 608002, Tamil Nadu, India Corresponding author Venkateswaran Chidambaram Seshadri, Department of Pharmacy, Annamalai University, Annamalai Nagar, Chidambaram, Pin 608002, Tamil Nadu, India E-mail:[email protected] Phone: 09840549751 Copy right © 2013 This is an Open Access article distributed under the terms of the Indo American journal of Pharmaceutical Research, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited. ARTICLE INFO ABSTRACT Article history Received 23/12/2013 Available online 31/12/2013 Keywords Disulfiram, Milling, Micronization, Aqueous wet granulation, Bioequivalence under Fasting. Tetraethylthiuram disulphide is chemical name of Disulfiram. There are few manufacturers available worldwide involved in the manufacture of Disulfiram Tablets due to its high bio variability from patient to patient. Disulfiram is available as immediate release tablets and effervescent / dispersible tablets. There is a report of high bio variability between the marketed, effervescent / dispersible tablets vis a vis immediate release tablets. Moreover, with respect to manufacturing of disulfiram tablets, the manufacturing process followed worldwide involves dry granulation by roller compaction / slugging method. The tablets thus prepared have very poor mechanical strength; rough edges are observed around the tablet circumference; when the marketed tablets are subjected to friability testing, tablets are failing in friability test owing to capping; some set of tablets show % friability in the range of 0.6- 0.85% with severe edge wearing. To overcome this problem, a set of manufacturers perform the blend compression by extending the dwell time to prevent capping of tablets. Another set of manufacturers make the tablets with co-processed excipients. In some of the marketed product, Tween 80 or Myrj 52 is used as wetting agent, which may intervene with the P-gp efflux mechanism precipitating high bio variability of Disulfiram. In the present research, Disulfiram Tablets were manufactured by aqueous wet granulation process. Manufactured tablets showed good morphology and mechanical strength, without tableting issues. In this research apart from robust manufacturing process, influence of milling and micronization of API on the in vivo bio variability of the drug was studied and reported. Please cite this article in press as Venkateswaran Chidambaram Seshadri,et al. Formulation and evaluation of tetraethylthiuram disulphide tablets by aqueous wet granulation process .Indo American Journal Of Pharm Research.2013:3(12).
Transcript

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Indo American Journal of Pharmaceutical Research, 2013 ISSN NO: 2231-6876

Journal home page:

http://www.iajpr.com/index.php/en/

INDO AMERICAN

JOURNAL OF

PHARMACEUTICAL

RESEARCH

FORMULATION AND EVALUATION OF TETRAETHYLTHIURAM DISULPHIDE

TABLETS BY AQUEOUS WET GRANULATION PROCESS

Venkateswaran Chidambaram Seshadri, Packiaraj Jeyachandran Manohari, Janakiraman

Kunchithapatham Department of Pharmacy, Annamalai University, Annamalai Nagar, Chidambaram, Pin – 608002, Tamil Nadu, India

Corresponding author

Venkateswaran Chidambaram Seshadri,

Department of Pharmacy,

Annamalai University, Annamalai Nagar,

Chidambaram, Pin – 608002, Tamil Nadu, India

E-mail:[email protected] Phone: 09840549751

Copy right © 2013 This is an Open Access article distributed under the terms of the Indo American journal of Pharmaceutical

Research, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.

ARTICLE INFO ABSTRACT

Article history

Received 23/12/2013

Available online

31/12/2013

Keywords

Disulfiram,

Milling, Micronization,

Aqueous wet granulation,

Bioequivalence under Fasting.

Tetraethylthiuram disulphide is chemical name of Disulfiram. There are few manufacturers

available worldwide involved in the manufacture of Disulfiram Tablets due to its high bio

variability from patient to patient. Disulfiram is available as immediate release tablets and

effervescent / dispersible tablets. There is a report of high bio variability between the

marketed, effervescent / dispersible tablets vis a vis immediate release tablets. Moreover, with

respect to manufacturing of disulfiram tablets, the manufacturing process followed worldwide

involves dry granulation by roller compaction / slugging method. The tablets thus prepared

have very poor mechanical strength; rough edges are observed around the tablet

circumference; when the marketed tablets are subjected to friability testing, tablets are failing

in friability test owing to capping; some set of tablets show % friability in the range of 0.6-0.85% with severe edge wearing. To overcome this problem, a set of manufacturers perform

the blend compression by extending the dwell time to prevent capping of tablets. Another set

of manufacturers make the tablets with co-processed excipients. In some of the marketed

product, Tween 80 or Myrj 52 is used as wetting agent, which may intervene with the P-gp

efflux mechanism precipitating high bio variability of Disulfiram. In the present research,

Disulfiram Tablets were manufactured by aqueous wet granulation process. Manufactured

tablets showed good morphology and mechanical strength, without tableting issues. In this

research apart from robust manufacturing process, influence of milling and micronization of

API on the in vivo bio variability of the drug was studied and reported.

Please cite this article in press as Venkateswaran Chidambaram Seshadri,et al. Formulation and evaluation of tetraethylthiuram

disulphide tablets by aqueous wet granulation process .Indo American Journal Of Pharm Research.2013:3(12).

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INTRODUCTION

Tetraethylthiuram disulphide is chemical name of Disulfiram. Disulfiram is an alcohol deterrent used for the treatment of

chronic alcoholism. Apart from the treatment of alcoholism it is being studied for the treatment of cocaine dependence. Disulfiram is

also useful in the treatment of Giardia infection and Scabies. Disulfiram has good activity against metronidazole resistant

Trichomonas vaginalis. Disulfiram creates dithiocarbamate complexes with metals which is a proteasome inhibitor. A clinical trial of

Disulfiram with copper gluconate against liver cancer is being conducted in Utah. A clinical trial in Israel evaluates the Disulfiram as

adjuvant against liver cancer. Currently, Disulfiram is the subject of research for use as a treatment in HIV cure through activating the

reservoir of HIV-infected resting CD4 cells. Recently a report suggests the role of Disulfiram as a P-gp efflux pump modulator;

Disulfiram inhibits ATP hydrolysis and binds to drug substrate binding sites of multiple ABC transporters which are associated with

drug resistance and is thus potentially an attractive agent to combat multidrug resistance. Disulfiram also possess the potentialas an antifungal agent. In a recent research, Disulfiram was screened for its antifungal potential on a spectrum of 61 fungal isolates. MIC50

and MIC90 of Disulfiram is better than Fluconazole, Amphotericin B, Itraconazole, Voriconazole and Cancidas in the case of Candida

parapsilosis, C. krusei, C. albicans, C. tropicalis, C. glabrata, Aspergillus fumigatus, A. flavus and A.niger. Disulfiram was also found

to be active against non-Candida yeast like Cryptococcus neoformans and Histoplasma capsulatum. Further, azoles are fungistatic in

nature whereas Disulfiram showed fungicidal activity against the tested fungal cultures of Candida parapsilosis, C. krusei, C. albicans,

C. tropicalis, C. glabrata, Aspergillus fumigatus, Cryptococcus neoformans and Histoplasma capsulatum. Antifungal potential of

Disulfiramwas tested against 13 Aspergillus isolates. Like amphotericin B, Disulfiram showed fungicidal potential activity with MIC50

and MIC90 of 2 and 8 µg /ml respectively. Disulfiram also has beneficial effect on symptoms caused by a lack of Vitamin E. Early

research has showed that certain dental diseases caused by lack of Vitamin E could be cured by Disulfiram. Disulfiram is a cream-

white colored, odourless, slightly bitter tasting, crystalline powder, practically insoluble in water, 0.02 g / 100 mL. Disulfiram readily

diffuses into cells and raise the intracellular thiol levels and hence can act on intracellular redox reactions. Disulfiram also has the ability to inhibit the xanthine oxidase and succinoxidase enzyme systems. Disulfiram also possess antithyroid action due to the NCS

group in its structure, which is common to many antithyroid compounds, probably producing stable complex through reaction with

free iodine. Disulfiram is rapidly absorbed from the gastrointestinal tract but the absorption is incomplete and about 20% is excreted

in the faeces. Disulfiram has high lipid solubility, hence widely distributed and accumulated in various fat depots. Disulfiram is a

prodrug which is rapidly metabolized to diethylthiocarbamate (DDC), and formed DDC is partly excreted as CS2 (carbon disulphide)

in the expired air through lungs and is partly metabolized in the liver to Me-DDC. Further, Me-DDC is metabolized to the active

metabolite MeDTC (diethylthiocarbaminic acid methyl ester). The concentration of Me-DTC reaches maximum after about 4 hours,

but the maximum enzyme-inhibiting effect (ALDH) is first reached (steady state) after 3 daily doses. The t1/2 for Me-DTC is about 10

hours, but the enzyme inhibiting effect of ALDH lasts significantly longer. Metabolism is not affected by a mild to moderate reduction

in liver function. On the contrary, in presence of liver cirrhosis an increased concentration of the metabolites is seen in the blood. The

metabolites are mainly excreted in the urine. Part is recovered in the expired air in the form of CS2 (Carbon Disulphide). About 20%

of administered dose may remain in the body for one week or longer. [1-20] The aim of the research is to make Disulfiram Tablets which will exhibit a better mechanical strength and morphology as compared to the marketed product. Disulfiram being a highly

variable drug, this research will also focus on the influence of milling and micronization of API on bioavailability of the drug product

and accordingly particle size specification of API will be finalized. Disulfiram API exhibits poor flow and compressibility. Direct

blending and compression process was not selected. Dry granulation and slugging method was not selected since the marketed product

samples made with the slugging process showed rough edges around the tablet circumference; when the marketed tablets are subjected

to friability testing, tablets are failing in friability test owing to capping; some set of tablets show % friability in the range of 0.6-

0.85% with severe edge wearing. Hence it was decided to formulate the Disulfiram tablets by aqueous wet granulation method.

Hydroxypropyl cellulose (Klucel LF) was selected as binder. Silicified Microcrystalline Cellulose (Prosolv SMCC HD 90) was

selected as diluent. Sodium Starch Glycolate Type A (Primojel) was selected as disintegrant. Colloidal Silicon Dioxide (Aerosil 200)

was selected as glidant and antistatic agent. Stearic Acid (Stellipress 1200 Poudre) and Non Bovine Grade Magnesium Stearate

(Tablube) were selected as lubricants.

MATERIALS AND METHODS

Excipients & Reagents

Disulfiram was obtained from Farchemia, Italy; Silicified Microcrystalline Cellulose (Prosolv SMCC HD 90) was obtained

from JRS Pharma Germany; Sodium Starch Glycolate Type A (Primojel) was obtained from DFE Pharma Germany; Hydroxypropyl

Cellulose (Klucel LF) was obtained from Ashland Inc USA; Non Bovine Grade Magnesium Stearate (Tablube) was obtained from

Nitika Chemicals India; Colloidal Silicon Dioxide (Aerosil 200) was obtained from Evonik Germany; Stearic Acid (Stellipress 1200

Poudre) was obtained from Stearinerie Dubois FIIs France; Sodium Lauryl Sulphate (Stepanol WA100) was obtained from Stephane

USA; Ethanol and Methanol were obtained from Avantor Performance Materials, India; Potassium Dihydrogen Phosphate, Potassium

Hydroxide were obtained from Merck Specialities Ltd India.

Equipments& Instruments High Shear Mixer Granulator 10 Litres manufactured by Kevin Process Technologies Private Limited; Fluid Bed Dryer

Processor & Granulator GPCG 1.1 manufactured by Pam Glatt Technology Limited; 16 Station Single Rotary Tablet Compression

Machine manufactured by Cadmach Machinery; Hardness Tester Type: TBH 125 manufactured by Erweka; Disintegration Test

Apparatus Model ED 2L manufactured by Electrolab; Thickness Tester Vernier Caliper Absolute Digimatic manufactured by

Mitutoyo; Friabilator EF-1W manufactured by Electrolab; Electromagnetic Sieve Shaker EM8-08 Plus manufactured by Electrolab;

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Tap Density Testing Apparatus ETD-1020 manufactured by Electrolab; Bottle Sealing Machine (Induction Cap Sealer) Sigma Flex

manufactured by Electronic Devices; Double Cone Blender with interchangeable bowls of 5L, 15L and 25L manufactured by Sams

Technomech; Loss On Drying Mositure Analyzer Model MB 45 manufactured by Ohaus; Multi Mill equipped with 1.5 mm screen

manufactured by Sams Technomech; Comminuting Mill equipped with 0.25 mm screen manufactured by Cadmach Machinery; MC

JetMill®50 manufactured by Dietrich Engineering Consultants, Switzerland; 40°C / 75% RH Stability Chamber manufactured by

Thermolab Scientific Equiments; HPLC manufactured by Waters; Vibrosifter manufactured by Gansons Engineering; 12.8 mm Round

Shaped Standard Concave Punch Tooling manufactured by ACG PAM Pharma Technology; Weighing Machine PS6000/C/1

manufactured by LCGC RADWAG; pH Meter H12215 manufactured by Hanna Instruments; Lab Stirrer RQ-126D manufactured by

Remi; Dissolution Apparatus TDT-08L manufactured by Electrolab;

Disintegration and Dissolution Parameters

Disintegration test was performed in USP disintegration test apparatus in Purified Water @ 37 ± 0.5°C. Specification: NMT

15 minutes. Dissolution was performed in 900 mL Purified Water with 2% Sodium Lauryl Sulphate. The parameters include, USP-II

(Paddle), 100 RPM. Time Points: 15, 30, 45, 60, 75, 90, 105 and 120 minutes. λmax at 254 nm. Specification: NLT 75 % (Q) of the

labeled amount in 120 minutes.

Method For Assay, Blend Uniformity, Content Uniformity / Uniformity of Dosage Units and Dissolution

Disulfiram is official in USP and the same method was utilized for the determination of Assay, Related Substances, Blend

Uniformity, Content Uniformity / Uniformity of Dosage Units and Dissolution

Method For Bulk Density, Tapped Density, Repose Angle and Friability Measurements USP guidelines followed in the measurement of Bulk Density, Tapped Density, Compressibility Index, Hausner Ratio,

Repose Angle and % Friability measurements.

Experimental/ Methodology

Marketed Product Characterization

Antabuse®(Disulfiram) Tablets 250 mg and 500 mg manufactured by Duramed Pharmaceuticals Inc. Subsidiary of Barr

Pharmaceuticals Inc. USA was characterized with respect to Inactive ingredients details, Weight, Thickness, Diameter, Disintegration

Time and Dissolution Profile and Packaging configuration.

API Characterization

Disulfiram was characterized with respect to Description, Bulk Density, Tapped Density, Compressibility Index, Hausner

Ratio, Repose Angle and Particle Size Distribution.

Drug-Excipient Compatibility Study

The possibility of drug-excipient interaction was investigated by HPLC analysis. Drug excipient compatibility study was

performed with excipients mentioned above (See ‘Excipients & Reagents’). Study was conducted by preparing homogenous mixture

of excipient with drug filled in glass vials were exposed to 40 ± 2°C / 75 ± 5%RH and 60°C for 4 weeks and 2 weeks respectively.

Samples were analysed for Assay, Total Impurity and Water By Kf.

Formulation

The Hydroxypropyl Cellulose (Klucel LF) required for the batch was divided into two parts, 70% of the total batch quantity

of Hydroxypropyl Cellulose (Klucel LF) was dissolved in terms of 12% w/w solids in Purified Water as a binder solution. The

remaining 30% of the total batch quantity of Hydroxypropyl Cellulose (Klucel LF) was sifted along with Disulfiram and Sodium Starch Glycolate (Primojel) through # 20 ASTM sieve. The sifted materials were charged in High Shear Mixer Granulator and dry

mixed at high impeller and chopper speed for 15 minutes. The dry mixed materials were granulated with binder solution of

Hydroxypropyl Cellulose (Klucel LF) at high impeller and chopper speed. The binder solution container was rinsed with purified

water which is 12% of the total quantity of binder solution prepared and rinsings were added to the contents of High Shear Mixer

Granulator. The wet granules were dried in Fluid Bed Dryer Processor & Granulator at 50°C till LOD is not less than or equal to 1%.

The dried granules were milled through Multi Mill equipped with 1.5 mm screen at fast speed knife forward configuration. The milled

granules were blended in Double Cone Blender at 15 RPM for 5 minutes. The extra granular materials except lubricants was sifted

through #20 ASTM sieve and blended along with granules of intragranular part in a Double Cone Blender at 15 RPM for 15 minutes.

The lubricants were sifted through #40 ASTM sieve and blended with the blended materials in a Double Cone Blender at 15 RPM for

5 minutes. The blend thus prepared was compressed into tablets using 12.8 mm Round Shaped Standard Concave Punch Tooling. The

details of Formulation Prototypes are shown in Table 1. The drying parameters are as follows,

Inlet Air Temperature – 50° +5°C; Exhaust Temperature – 40°+5°C; Filter Shaking Interval – 20 ± 5 seconds; Shaking Duration – 5 ± 1 second; Shaking Mode – Auto

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Table 1.Formulation of Prototypes

S.No Ingredients A B C D E F

mg / tablet

Intragranular Ingredients

1 Disulfiram (Milled) 500.00 500.00 500.000 500.000 500.00 -

2 Disulfiram (Micronized) - - - - - 500.00

3 Sodium Starch Glycolate Type A (Primojel) 10.00 10.00 10.000 22.500 35.00 35.00

4 Hydroxypropyl Cellulose (Klucel LF) 30.00 30.00 20.000 20.00 20.00 20.00

5 Purified Water QS QS QS QS QS QS

Total Intragranular Ingredients 540.00 540.00 530.000 542.500 555.00 555.00

Extragranular Ingredients

6 Silicified Microcrystalline Cellulose (Prosolv SMCC HD 90)

137.00 130.00 140.000 111.500 99.00 99.00

7 Sodium Starch Glycolate Type A (Primojel) 8.00 8.00 8.000 16.000 16.00 16.00

8 Colloidal Silicon Dioxide (Aerosil 200) 8.00 8.00 8.000 16.000 16.00 16.00

9 Stearic Acid (Stellipress 1200 Poudre) 6.00 12.00 12.000 12.000 12.00 12.00

10 Magnesium Stearate (Tablube) 1.00 2.00 2.000 2.000 2.00 2.00

Total Extragranular Ingredients 160.00 160.00 170.000 157.500 145.00 145.00

Total Tablet Weight 700.00 700.00 700.000 700.000 700.00 700.00

EVALUATION

The blend of all prototypes was characterized with respect to LOD, Repose Angle, Bulk / Tapped Density, Hausner Ratio and

PSD. Prepared Tablets were characterized with respect to Weight, Thickness, Hardness, Friability, Disintegration Time and

Dissolution Profile.

Stability Studies

The finalized formulation of all strengths was subjected to accelerated stability study at 40±2°C / 75±5% RH. 100 Tablets

were packed in 150 cc HDPE bottle with 38 mm Child Resistant Cap with cotton as dunnage and induction sealed. Description,

Disintegration Time, Dissolution, Assay and Related Substances were studied during stability. In case of dissolution, method followed

was USP-II (Paddle), 100 RPM, 900 mL, Purified Water with 2% Sodium Lauryl Sulphate @ 37 ± 0.5°C. Time Points: 15, 30, 45, 60,

75, 90, 105 and 120 minutes. Specification: NLT 75 % (Q) of the labeled amount in 120 minutes.

In vivo Studies

An open-label, balanced, randomized, three-treatment, three-period, three-sequence, single-dose, crossover, bioequivalence

study of Disulfiram Tablets, 500 mg (made with micronized API – Test 1), Disulfiram Tablets, 500 mg (made with milled API - Test

2), with that of Reference product, Antabuse® (Disulfiram) Tablets 500 mg was conducted in 15 healthy adult human subjects under fasting condition. The study protocol was prepared and approval from Independent Ethical Committee – The Ethical Jury, Chennai

was obtained. The studies were conducted in compliance with the ethical principles of the Declaration of Helsinki, the International

Conference on Harmonization’s Good Clinical Practices guidelines and the guidelines of Indian Council of Medical Research for

Biomedical Research on Human Subjects and Good Clinical Practices for Clinical Research in India. Study subjects were screened

and enrolled for the study. Enrolled subjects were housed in the clinical facility for 11 hours prior to drug administration until 24

hours post dose. In case of study under fasting condition, after overnight fasting of at least 10 hours, a single oral dose of either tests or

reference product was administered to the subjects and to swallow it with about 240 mL of water in sitting posture. Then the subject

will be fasted for at-least 4 hours post dosing. The pre-dose 0 hour blood sample was collected before dosing and post dose samples

were collected at 0.5, 1.0, 1.5, 2.0, 2.5, 3.0, 3.5, 4.0, 4.5, 6.0, 6.5, 7.0, 8.0, 10.0, 12.0, 16.0, 24.0, 36.0, 48.0 and 72.0 hours. Subjects were

provided standard diet and continuously monitored for well-being and safety throughout the study. The concentration of S-methyl

N,N-diethyldithiocarbamate (Me-DDC), which is an active metabolite of Disulfiram in plasma samples were analysed using validated analytical method. Pharmacokinetic and statistical analyses were performed on obtained drug concentration data. Healthy, willing

human volunteers between 18 and above were selected on the basis of medical history, physical examination (including but may not

be limited to an evaluation of the cardiovascular, gastrointestinal, respiratory and central nervous systems) vital sign assessments, 12-

lead electrocardiogram (ECG), X-ray, and clinical laboratory assessments, urine screen for drugs of abuse and alcohol breath test.

Informed consent was obtained from the subjects after explaining the nature and purpose of the study. Pharmacokinetic analysis was

performed using WinNonlin® software version: 5.3 of Pharsight Corporation, USA for the following pharmacokinetic parameters

Cmax, AUC0-t, AUC0-∞, Tmax, Kel, , t½ , Kel_Lower, Kel_Upper and AUC_%Extrap_obs. Analysis of variance (ANOVA)

consistent with two one-sided test for bioequivalence, ratio analysis and 90% confidence intervals for ratio of least square mean of Ln-

transformed data of Cmax, AUC0-t and AUC0-∞ for tests and reference products were calculated by using SAS® statistical software

version 9.1.3 from SAS Institute Inc, USA. For Disulfiram, in terms of S-methyl N,N-diethyldithiocarbamate (Me-DDC), which is an

active metabolite of Disulfiram, the 90% confidence interval of the relative mean Cmax, AUC0-t and AUC0-∞ of the tests and

reference product should be between 80.00% and 125.00% for log-transformed data.

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RESULTS AND DISCUSSION

Marketed Product Characterization

Weight, Thickness, Diameter, Disintegration Time, Dissolution Profile and Packaging configuration details of

Antabuse®(Disulfiram) Tablets, 250 mg and 500 mg are provided in Table 2. Both the strengths of the marketed product are dose

proportional in design. Hence it was decided to formulate the higher strength and the same formula composition with half of it will be

used for preparing the lower strength.

API Characterization

Description, Bulk Density, Tapped Density, Compressibility Index, Hausner Ratio, Repose Angle and Particle Size

Distribution of API was done and the details are provided in Table 3.Compressibility Index, Hausner Ratio and Flow property of API is poor and needs to be improved through formulation.

Drug-Excipient Compatibility Study

Drug Excipient compatibility data shown in Table 4. suggests that both the temperature and moisture doesn’t affect the

stability of mixture indicating compatibility of drug with excipients studied.

Table 2. Marketed Product Characterization. Mean ± SD

Particulars 250 mg 500 mg

Description

White round, scored tablets debossed

OP 707 on one side and scored on the

other side.

White round, scored tablets debossed

OP 706 on one side and plain on the

other side.

Excipients Colloidal Silicon Dioxide, Anhydrous Lactose, Magnesium Sterarate, Microcrystalline

Cellulose, Sodium Starch Glycolate and Stearic Acid Diameter 10.38 mm Round Standard Concave 12.76 mm Round Standard Concave

Weight (mg) 380.6±1.57 781.4±1.89

Thickness (mm) 4.72±0.03 6.15±0.01

Hardness (kP) 5.6±0.80 12.0±0.45

% LOD 1.11% 1.17%

Disintegration Time 55 secs ±0.2 1 min 55 secs ± 0.3

Time (min) Dissolution (mean % drug dissolved) n=6 units

15 41.1±1.4 51.6±0.4

30 57.9±1.3 62.5±0.4

45 68.6±1.3 70.8±1.1

60 74.5±1.4 74.4±0.6

75 79.3±1.6 77.5±0.6 90 82.5±1.7 79.9±0.8

105 84.3±1.8 81.4±0.7

120 87.3±1.8 83.3±0.9

Pack Details

100 Tablets in 100 cc HDPE Bottle with

cotton coils as dunnage capped with 38 mm

Polypropylene Child Resistant Cap with

induction seal liner

100 Tablets in 100 cc HDPE Bottle with

cotton coils as dunnage capped with 38 mm

Polypropylene Child Resistant Cap with

induction seal liner

Table 3.API Characterization

Particulars Details

Description White to off-white crystalline powder

Bulk Density 0.51 g / ml

Tapped Density 0.77 g / ml

Compressibility Index 34% Hausner Ratio 1.51

Repose Angle 39.3°

Particle Size Distribution

By Malvern Mastersizer®

For API from Manufacturer d10 20.48 microns, d50 60.93 microns & d90 171.07 microns

For Milled API d10 12.47 microns, d50 42.83 microns & d90 83.33 microns

For Micronized API d10 2.33 microns, d50 6.57 microns & d90 12.38 microns

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Table.4 Drug-Excipient Compatibility Study

Note:TI – Total Impurity; % Moisture determined by Water by Kf.

FORMULATION

For the prototype Batches A to E, milled API was used and the granulation, drying, milling, prelubrication and lubrication

blending time were kept constant. The blend prepared was compressed with uniform hardness into tablets. Blend of batch A showed

poor flow; disintegration time of tablets was more than 8 minutes; picking, sticking and striation were observed during blend

compression. To overcome the tableting issues of picking, sticking and striation, in batch B the concentration of Stearic Acid

(Stellipress 1200 Poudre) and Magnesium Stearate (Tablube) were doubled from 6 mg to 12 mg and 1 mg to 2 mg respectively. Blend

of batch B showed poor flow; disintegration time of tablets was more than 8 minutes; picking, sticking and striation were not observed

during blend compression. Increase in Disintegration time may be due to excess binder concentration, hence in batch C the

concentration of Hydroxypropyl Cellulose (Klucel LF) was reduced from 30 mg to 20 mg. Blend of batch C showed poor flow;

disintegration time of tablets has improved from 8 minutes to 6 minutes. To overcome the poor blend flow and slow disintegration

time of tablets, in batch D the concentration of Sodium Starch Glycolate Type A (Primojel) was increased from 10 mg to 22.5 mg in the intragranular part and 8 mg to 16 mg in the extragranular part; the concentration of Colloidal Silicon Dioxide (Aerosil 200) was

API + Excipients Tests Initial Duration / Storage Conditions

2nd

Week 60°C 4th

Week 40°C/75%RH

Disulfiram %ASSAY 99.94 100.61 103.77

%TI 0.054 0.044 0.045

%Moisture 0.2 0.1 0.0

Disulfiram+

Hydroxypropyl Cellulose (1:1)

%ASSAY 97.81 95.98 100.67

%TI 0.057 0.052 0.045

%Moisture 1.32 1.21 1.6

Disulfiram+ Lactose

Anhydrous (1:1)

%ASSAY 88.63 89.06 89.45

%TI 0.050 0.047 0.035

%Moisture 2.16 2.23 2.01

Disulfiram+ Crospovidone

(1:1)

%ASSAY 92.76 92.99 94.44

%TI 0.054 0.047 0.047

%Moisture 1.6 1.54 1.75

Disulfiram+ Microcrystalline Cellulose (1:1)

%ASSAY 93.42 96.07 95.17

%TI 0.058 0.040 0.042

%Moisture 0.83 0.92 0.74

Disulfiram+Sodium Starch

Glycolate (1:1)

%ASSAY 99.88 100.43 99.33

%TI 0.052 0.047 0.040

%Moisture 1.99 1.86 2.02

Disulfiram+

CroscarmelloseSodium(1:1)

%ASSAY 95.08 97.18 97.93

%TI 0.054 0.041 0.047

%Moisture 3.8 2.6 3.88

Disulfiram+Pregelatinized

Starch (1:1)

%ASSAY 84.37 83.26 83.65

%TI 0.048 0.046 0.038

%Moisture 2.03 2.03 3.37

Disulfiram+ Microcrystalline Cellulose

(1:1)

%ASSAY 102.25 97.85 101.75

%TI 0.057 0.034 0.048

%Moisture 0.25 0.26 0.38

Disulfiram+Colloidal Silicon

Dioxide (1:1)

%ASSAY 101.70 102.91 104.96

%TI 0.054 0.064 0.047

%Moisture 0.19 0.14 0.51

Disulfiram+Magnesium

Stearate (1:1)

%ASSAY 100.87 98.07 101.53

%TI 0.052 0.041 0.053

%Moisture 0.24 0.29 0.38

Disulfiram+Stearic Acid (1:1) %ASSAY 96.06 95.76 96.30

%TI 0.055 0.040 0.045

%Moisture 0.22 0.11 0.19

Disulfiram+SodiumStearylFum

arate (1:1)

%ASSAY 99.02 100.23 99.85

%TI 0.060 0.045 0.048

%Moisture 0.12 0.0 0.0

Disulfiram+

Ultramicronized Talc (1:1)

%ASSAY 101.22 102.85 101.80

%TI 0.054 0.044 0.043

%Moisture 0.26 0.25 0.23

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increased from 8 mg to 16 mg in the extragranular part. Blend of batch D showed good flow and the disintegration time of tablets has

improved from 6 minutes to 4 minutes. To further improve the disintegration time of tablets, in batch E the concentration of Sodium

Starch Glycolate Type A (Primojel) in the intragranular part was increased from 22.5 mg to 35 mg. Tablets of Batch E showed

disintegration time of about 2 minutes. Blend and Tablet characteristics of Batch E was found to be optimal. The same composition

was used for the preparation of Disulfiram Tablets (Batch F) manufactured with Disulfiram (Micronized) API. With the composition

of batch E, Disulfiram Tablets were manufactured and the process parameters were optimized. The characterization study for blend

and tablets were done and are summarized in Table 5. In Batch E, Blending time optimization study was taken up as part of process

optimization study. Blending time optimization involves two stages of study, Prelubrication blending time and Lubrication or final

blending time. In Prelubrication blending time, the sifted extra granular ingredients except lubricant were blended along with blended

milled granules in double cone blender at 15 RPM, the blend uniformity samples were sampled in duplicate at different location in the blender at the end of 10 minutes, 15 minutes and 20 minutes. In the lubrication or final blending time the sifted lubricants were

blended along with the blended materials in the double cone blender at 15 RPM, the blend uniformity samples were sampled in

duplicate at different location in the blender at the end of 4, 5 and 6 minutes. See Table 6 for details. Based on the blend uniformity

data, blending time of 15 minutes was finalized for the Prelubrication stage and blending time of 5 minutes was finalized for the

lubrication stage. This optimized blending time will be followed in the manufacturing process of lower strength, 250 mg. After

blending time optimization study, compression process was optimized with respect to turret speed (RPM) and hardness variation

study. Turret speed and its influence on the prepared tablets were characterized by weight variation and content uniformity, based on

the results the turret speed range was finalized. In hardness variation study, the tablets are compressed at different hardness range and

the influence of the same on thickness variation, % friability, disintegration time and dissolution were studied and accordingly a

suitable hardness range was finalized.

Table 5. Blend and Tablet Characterization. Mean ± SD

Particulars

A B C D E F

Dry Mix Time(min) 15 15 15 15 15 15

Dry Mix LOD (%) 0.96 0.78 0.68 0.77 0.92 0.62

Dry Mix Bulk Density ( g / ml) 0.17 0.14 0.19 0.17 0.14 0.14

% Granulation Binder Uptake 42 42 42 42 42 42

Kneading Time (min) 3 3 3 3 3 3

Total Granulation Time (min) 24 24 24 24 24 24

Drying Time in FBP (min) 19 23 21 19 18 22

LOD of Dried Granules (%) 0.90 0.78 0.58 0.88 0.64 0.94

Prelubrication Blending (min) 15 15 15 15 15 15

Lubrication Blending (min) 5 5 5 5 5 5 Bulk Density (g/ml) 0.57 0.55 0.67 0.41 0.54 0.52

Tapped Density (g/ml) 0.95 0.92 1.07 0.67 0.74 0.70

Compressibility Index (%) 39.8 40.5 37.5 38.7 27.0 25.4

Hausner Ratio 1.66 1.68 1.60 1.63 1.37 1.34

LOD of Final Blend (%) 1.46 1.17 1.89 1.82 1.32 1.28

Repose Angle (°) 39.2 36.5 38.6 29.1 29.6 29.4

Turret Speed (RPM) 20 20 20 20 20 20

Average Weight (mg) 703.9±4.51 696.5±3.01 703.5±7.52 703.2±7.05 701.3±5.50 701.1±7.02

Average Thickness (mm) 6.08±0.28 6.03±0.26 6.02±0.29 6.02±0.25 6.05±0.24 6.04±0.21

Average Hardness (kP) 9-21 9-21 9-21 9-21 9-21 9-21

Friability (%) 0.35 0.33 0.35 0.34 0.38 0.25 Disintegration Time(mins) 8.02±1.27 8.42±1.14 6.07±1.23 4.21±1.18 2.20±1.38 3.15±1.83

Picking / Sticking /Striation

Sieve # (ASTM) Final Blend PSD (% Retained) 20 0 0 5 15 2 10

40 26.1 26.4 15 20 18 25

60 15.2 16.09 12.5 10 22 7.5

80 10.9 9.19 7.5 7.5 12 5

100 8.7 6.89 2.5 7.5 8 7.5

140 15.2 9.19 7.5 10 12 10

200 10.9 9.19 12.5 12.5 10 15

Pan 13.0 23.05 37.5 17.5 16 20

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Table 6. Prelubrication Blending Time & Lubrication Blending Time Optimization

Stage Prelubrication Stage Lubrication Stage

Time (mins) 10 15 20 4 5 6

Sample # Blend Uniformity (% Assay)

1 96.59 95.92 96.67 98.08 98.38 99.16

2 96.86 95.51 95.95 98.14 97.59 98.35

3 97.68 94.80 95.79 101.90 98.86 95.97

4 95.11 96.99 94.86 96.53 98.97 97.79

5 96.88 97.31 95.81 98.17 97.77 99.79

6 96.98 98.84 97.30 97.77 97.52 96.65

7 97.06 94.89 95.70 97.69 99.27 96.48 8 96.31 96.18 97.72 97.29 98.61 98.13

9 96.87 96.42 95.96 97.99 97.16 99.68

10 97.32 96.93 98.24 96.70 99.81 96.99

Average 96.76 96.37 96.40 98.02 98.39 97.89

Minimum 95.11 94.80 94.86 96.53 97.16 95.97

Maximum 97.68 98.84 98.24 101.90 99.81 99.79

% RSD 0.71 1.26 1.09 1.51 0.87 1.39

Turret Speed Study

The final blend of Batch E was compressed at different turret speed of 10 RPM, 20 RPM and 30 RPM. The tablets were

collected and checked for weight variation and content uniformity. The details are provided in Table 7. Irrespective of machine speed,

the weight variation and the content uniformity of the tablets compressed were within the specification limits; hence all the strengths

of Disulfiram tablets can be comfortably compressed at turret speed range of 10-30 RPM.

Hardness Variation Study

The final blend of Batch E was compressed at different hardness of 10 kP, 15 kP and 20 kP. The tablets were collected and

checked for hardness variation, thickness variation, % friability, disintegration time and dissolution. The details are provided in Table

8, 9 and 10. Irrespective of hardness variation studied, the thickness, hardness, % friability, disintegration time and dissolution of the

compressed were within the specification limits; hence all the strengths of Disulfiram tablets can be comfortably compressed at

hardness range of 10 to 20 kP.

Table 7. Turret Speed Optimization Study By Weight Variation & Content Uniformity. Mean ± SD

Particulars

Weight Variation (mg) Content Uniformity (% Assay)

Low Speed,

10 rpm

Target Speed,

20 rpm

High Speed,

30 rpm

Low Speed,

10 rpm

Target Speed,

20 rpm

High Speed,

30 rpm

Batch E

Average 703.9±2.41 699.7±3.20 696.1±4.8 97.1±1.46 96.5±1.32 98.8±1.48

Minimum 700.0 693.0 690.0 94.7 93.6 95.8 Maximum 709.0 703.0 704.0 99.1 99.2 101.0

Table 8. Hardness Optimization Study By Hardness Variation & Thickness Variation. Mean ± SD

Particulars

Hardness Variation (kP) Thickness Variation (mm)

Low Hardness,

10 kP

Target Hardness,

15 kP

High Hardness,

20 kP

Low Hardness,

10 kP

Target Hardness,

15 kP

High Hardness,

20 kP

Batch E

Average 11.2±0.50 15.3±0.70 21.0±0.75 6.25±0.09 6.08±0.07 5.90±0.06

Minimum 9.4 14.0 18.8 6.14 6.00 5.86

Maximum 12.7 17.6 22.8 6.32 6.14 5.98

Table 9. Hardness Optimization Study By % Friability & Disintegration Time. Mean ± SD

Particulars

% Friability Disintegration Time (minutes)

Low Hardness,

10 kP

Target Hardness,

15 kP

High Hardness,

20 kP

Low Hardness,

10 kP

Target Hardness,

15 kP

High Hardness,

20 kP

Batch E

Average

0.26 0.11 0.13

2.44±0.53 3.26±0.59 4.39±0.44

Minimum 2.12 3.04 4.17

Maximum 3.15 4.17 5.02

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Table 10. Hardness Optimization Study By Dissolution Profile. Mean ± SD

Particulars Hardness

Variation (kP)

Mean % Dissolved (n=6 units)

Time (Minutes)

15 30 45 60 75 90 105 120

Batch E

10 53.6±3.4 77.6±1.0 85.7±0.7 90.7±0.9 92.4±0.9 94.2±0.1 96.3±0.6 97.0±0.5

15 51.3±2.4 77.6±0.9 88.3±0.6 92.3±0.3 96.5±0.5 98.3±0.7 100.0±0.5 100.4±0.5

20 54.9±3.6 82.2±0.1 88.4±0.1 94.3±0.4 96.3±0.9 98.9±0.4 100.6±0.9 101.4±0.9

Medium: 900 ml, Purified water @ 37 ± 0.5ºC, USP-II (Paddle), 100 RPM, Specification: NLT 75% (Q) in 120 minutes

Dissolution Profile Comparison of Test Product Vs Marketed Product

Dissolution profile of the prepared tablets of Disulfiram was compared against the marketed product, Antabuse®(Disulfiram)

Tablets, 500 mg. The dissolution profiles of both Batch E (Milled API) and Batch F (Micronized API) were on the higher side except

the 15th minute time point as compared to the marketed product Antabuse®(Disulfiram) Tablets, 500 mg. The extent of drug release of the prepared tablets was better as compared to the marketed product. At the end of 120 minutes, the test products showed drug release

of about 100% whereas the marketed product showed about 83% drug release. Both the test products complied to the dissolution

specification of not less than 75% (Q) in 120 minutes. See Table 11 and Figure 1 for further details.

Table 11. Dissolution Profile Comparison of Test Products Vs Marketed Product. Mean ± SD

Particulars

Mean % Dissolved (n=6 units)

Time (Minutes)

15 30 45 60 75 90 105 120

Antabuse® 51.6±0.4 62.5±0.4 70.8±1.1 74.4±0.6 77.5±0.6 79.9±0.8 81.4±0.7 83.3±0.9

Batch E (API Milled) 51.3±2.4 77.6±0.9 88.3±0.6 92.3±0.3 96.5±0.5 98.3±0.7 100.0±0.5 100.4±0.5

Batch F (API Micronized) 66.5±1.6 83.8±0.3 91.1±0.1 95±0.1 97.3±0.5 98.5±0.8 99.6±0.8 100.1±0.6

Medium: 900 ml, Purified water @ 37 ± 0.5ºC, USP-II (Paddle), 100 RPM, Specification: NLT 75% (Q) in 120 minutes

Figure 1. Dissolution Profile Comparison of Batch E (Milled API) & Batch F (Micronized API) Vs

Antabuse® (Disulfiram) Tablets, 500 mg

Stability Study

The prepared Disulfiram tablets of Batch E (Milled API) and Batch F (Micronized API) were packed in terms of 100 tablets

per 150 cc HDPE bottle and capped with 38 mm child resistant polypropylene closure with Cotton coil as dunnage and sealed with

induction seal liner. The packed induction sealed bottles were subjected to accelerated stability study at 40°C / 75% RH for 3 months

and the prepared drug product was found to be stable. See Table 12 for further details.

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Table 12. Stability Results at 40°C ± 2°C / 75 ± 5% RH. Mean ± SD

Batch E (Milled API)

Test Specification Initial 1st Month 2

nd Month 3

rd Month

Disintegration Time (minutes) NMT 15 minutes 3.26±0.59 3.38±0.61 3.24±0.32 3.29±0.47

Dissolution [mean±SD] NLT 75%(Q)

in 120 minutes 100.4±0.50 99.1±0.34 100.2±0.41 98.7±0.51

Assay (%) 90-110 99.9 99.1 98.1 99.4

Related Substances (%)

Highest Unknown Impurity NMT 0.24 0.044 0.027 0.053 0.072

Total Impurities NMT 1.0 0.108 0.076 0.111 0.126

Batch F (Micronized API)

Disintegration Time (secs) NMT 15 minutes 3.15±1.83 3.29±1.68 3.11±1.52 3.27±1.71

Dissolution NLT 75%(Q)

in 120 minutes 100.1±0.60 98.7±0.43 99.8±0.46 100.1±0.72

Assay (%) 90-110 100.9 99.8 101.0 99.6

Related Substances (%) Highest Unknown Impurity NMT 0.24 0.044 0.027 0.044 0.095

Total Impurities NMT 1.0 0.113 0.062 0.102 0.152

White to off-white colored, uncoated, round shaped biconvex tablets; on stability no morphological change observed.

In vivo Bioequivalence Study

In vivo studies were carried out for test formulations, Batch F (Mirconized API – Test 1) and Batch E (Milled API – Test 2)

against the reference product Antabuse® (Disulfiram) Tablets. The plasma levels of Disulfiram, in terms of S-methyl N,N-

diethyldithiocarbamate (Me-DDC), which is an active metabolite of Disulfiram was determined. The mean concentration-time profiles

for the marketed and test products of Disulfiram under fasted condition were shown in Table 13 and Figure 2 respectively. The Test

product – 1 made with micronized API was found to be bioinequivalent to the marketed product in terms of Cmax, AUC0-t and AUC0-∞. The T/R ratio of the test product-1 with respect to Cmax, AUC0-t and AUC0-∞was found to be 178.20%, 136.39% and 137.26%

respectively. The 90% Confidence Interval of the T/R ratio with respect to Cmax, AUC0-t and AUC0-∞ was found to be in range of

155.89 – 203.71%, 119.18 – 156.08% and 120.08 – 156.91% respectively. With respect to Tmax the test product-1 is 2.5 hours whereas

the Tmax of the reference product is 4.5 hours. Test product 1 made with micronized API reaches peak plasma concentration at a rapid

rate than the reference product. The particle size of micronized API d90 is 12.38 microns. Based on the bioequivalence results of test

product 1 against the reference product, Micronization of API causes rapid dissolution and the drug reaches the peak plasma

concentration within 2.5 hours. Hence for the formulation of Disulfiram tablets, micronization of API is not required. The Test

product – 2 made with milled API was found to be bioequivalent with the Reference product in terms of AUC0-t and AUC0-∞ and

bioinequivalent with respect to Cmax. The T/R ratio of the test product-2 with respect to Cmax, AUC0-t and AUC0-∞was found to be

123.27%, 108.10% and 108.45% respectively. The 90% Confidence Interval of the T/R ratio with respect to Cmax, AUC0-t and AUC0-∞

was found to be in range of 107.84 – 140.92%, 94.46 – 123.71% and 94.87 – 123.97% respectively. With respect to Tmax the test

product-2 is 4.5 hours exactly matching with the Tmax of the reference product which is also 4.5 hours. Test product 2 made with milled API reaches peak plasma concentration at a similar rate as that of the reference product. The particle size of milled API d90 is

83.33 microns. Based on the bioequivalence results of test product 2 against the reference product, Milling of API causes drug

dissolution and absorption at a similar as that of the reference product and the drug reaches the peak plasma concentration at 4.5 hours.

Hence for the formulation of Disulfiram tablets, milling of API is required to be bioequivalent with that of the reference product.

Regarding the bioinequivalence of Test product 2 with respect to Cmax against the reference product, the issue is precipitated because

of biovariability in plasma levels of Disulfiram, in terms of S-methyl N,N-diethyldithiocarbamate (Me-DDC), which is an active

metabolite of Disulfiram. On careful analysis of the pharmacokinetic data sheet of this study with respect to minimum, maximum and

% RSD values of Cmax of reference product vis a vis test product-2 the biovariability factor (Volunteer to volunteer) plays a major role.

The minimum, maximum and % RSD values of Cmax of reference product & test product–2 are 23.3109 ng/ml, 145.8652 ng/ml and

63.1063% & 23.0799 ng/ml, 112.7645 ng/ml and 38.1768% respectively. Based on the above facts, to achieve bioequivalence with

that of the reference product, Disulfiram tablets needs to be formulated with milled API and in the bioequivalence study, considering the biovariability of Disulfiram the number volunteers needs to be increased to reduce the intra subject variability for both the test and

reference product.

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Table 13 Statistical Analysis of Pharmacokinetic Data – Fasted Study

Product / Statistics Cmax

(ng / mL)

AUC0-t

(ng.h/ml)

AUC0-∞

(ng.h/ml)

Tmax

(h)

Test Product - 1

Arithmetic Mean 80.7731 957.5747 1007.1244

2.50 Geometric LS Mean 4.3423 6.8016 6.8524

Standard Deviation 28.2446 342.9588 358.2954

Test Product – 2 Arithmetic Mean 56.9497 772.9077 807.9112

4.50 Geometric LS Mean 3.9738 6.5692 6.6168

Standard Deviation 21.7416 283.3861 289.4438

Reference Product

Arithmetic Mean 48.8440 714.0690 748.7907

4.50 Geometric LS Mean 3.7646 6.4913 6.5357 Standard Deviation 30.8236 326.3148 351.0084

T / R Ratio

T1/R (%) 178.20 136.39 137.26

T2/R (%) 123.27 108.10 108.45

90% Confidence Interval (T1/R)

Lower Limit (%) 155.89 119.18 120.08

Upper Limit (%) 203.71 156.08 156.91

90% Confidence Interval (T2/R) Lower Limit (%) 107.84 94.46 94.87

Upper Limit (%) 140.92 123.71 123.97

ISCV (%)

21.73 21.91 21.73

Figure 2 Mean Concentration Time Profile – Fasted Study

CONCLUSION

Disulfiram tablets were successfully formulated by a simple aqueous wet granulation process. Disulfiram is an insoluble and

highly biovariable drug. Disulfiram drug product is available in 2 strengths in the market namely 250 mg and 500 mg. Tablet

morphology, mechanical strength, disintegration time and dissolution were fixed as prerequisite design attributes. Formulation was initiated for highest strength, 500 mg using milled API. Hydroxypropyl cellulose (Klucel LF) was selected as binder. Silicified

Microcrystalline Cellulose (Prosolv SMCC HD 90) was selected as diluent. Sodium Starch Glycolate Type A (Primojel) was selected

as disintegrant. Colloidal Silicon Dioxide (Aerosil 200) was selected as glidant and antistatic agent. Stearic Acid (Stellipress 1200

Poudre) and Non Bovine Grade Magnesium Stearate (Tablube) were selected as lubricants. The finalized prototype batch E showed

favorable blend and tablet characteristics. The disintegration and dissolution profile of the tablets were also found to be satisfactory.

The blend was characterized by determining bulk density, tapped density, hausner ratio, compressibility index, loss on drying, repose

angle and particle size distribution. Blending time optimization studies were taken in Batch E. Prelubrication blending time was

finalized at 15 minutes; Lubrication blending time was finalized at 5 minutes based on blend uniformity data at different time

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intervals. Further, turret speed optimization & hardness variation optimization was done and was characterized by determining weight

variation and content uniformity & hardness variation, thickness variation, % friability, disintegration time and dissolution

respectively. Based on the data, the turret speed was finalized in the range of 10-30 RPM and hardness was finalized in the range of

10-20 kP. After finalization of composition, the same formula was utilized for the formulation of Disulfiram tablets with micronized

API. Disulfiram tablets made with both milled and micronized API showed comparable disintegration and the dissolution profile to

the marketed product, ANTABUSE® manufactured by Duramed Pharmaceuticals Inc. Subsidiary of Barr Pharmaceuticals Inc. USA.

Disulfiram tablets made with both milled and micronized API were subjected to accelerated stability study in HDPE bottle pack and

the physico-chemical properties were found to be stable. The prepared Disulfiram tablets made with both milled and micronized API

was subjected to in vivo bioequivalence study under fast condition against the reference / marketed product, ANTABUSE®

manufactured by Duramed Pharmaceuticals Inc. Subsidiary of Barr Pharmaceuticals Inc. USA. Disulfiram Tablets made with milled API showed promising bioequivalence with that of the marketed product.

Future Research – In vivo bioequivalence study under fasting needs to be taken up with higher number of human volunteers to

reduce the biovariability and to establish the bioequivalence of Disulfiram Tablets made with milled API against the marketed product

ANTABUSE®.

Authors’ Statements

Competing Interests - The authors declare no conflict of interest.

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