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Pharmaceutical Technology: Controlled Drug Release, Volume 2

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44 CH. 4] STATISTICAL OPTIMIZATION OF A CONTROLLED RELEASE FORMULATION<br />

Two polymers were incorporated in the inert matrix system: ethylcellulose and polyvinyl<br />

chloride. The processes used to prepare tablets containing such polymers often include direct<br />

compression [4–6], wet granulation [7,8], coating [9–11] and, rarely, dry granulation [12].<br />

In previous work, the formula used were optimized by direct compression [13]. The area under<br />

the dissolution curve was optimized and validated by a composite design. However, the<br />

formulation gave poor powder flow as well as variability in the dissolution parameters. Thus the<br />

double compression process was investigated in order to change the powder into solid aggregates<br />

and therefore to enhance homogeneity, density and powder flow; in addition it was expected that<br />

this process would reduce the variability between tablets.<br />

Statistical optimization was conducted in three steps:<br />

(1) A Hadamard matrix H(8) was first applied to study the main effects of four parameters.<br />

(2) A 2 2 factorial design was built to obtain a complete linear model including only two<br />

parameters.<br />

(3) Validation of the mathematical model and then the optimum formulation were then made.<br />

MATERIALS<br />

The formula contained the drug, two inert matrices and two lubricants:<br />

Diclofenac sodium (Secifarma) 25.0%<br />

Ethylcellulose N-7 (Hercules) 26.1%<br />

PVC (Pevikon PE 737 P) (SEPPIC) 45.9%<br />

Magnesium stearate (Prophac) 1.0%<br />

Talc USP (Prophac) 2.0%<br />

METHODS<br />

The manufacturing process<br />

When using dry granulation, it is highly desirable to add a binder to the mixture in order to ensure<br />

an acceptable cohesion between particles. Therefore, in this present study, ethylcellulose was<br />

incorporated in two parts: before precompression as a binder, and before the final compression as<br />

an independent variable in the experimental design.<br />

The manufacturing process described below was followed:<br />

(1) Mixing for 5 min in a Turbula WAB (T2C, Willy A.Bachofen AG).<br />

(2) Precompression using a Frogerais 0A single-punch instrumented press (Ets. Ed. Frogerais),<br />

equipped with flat punches 11.28mm in diameter (surface area, 1 cm 2 ). The speed of the machine<br />

was adjusted to one tablet s −1 .<br />

(3) Milling was carried out in an Erweka oscillating granulator equipped with 3.15 mm<br />

perforations for premilling and 0.8mm perforations for the final milling.

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