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Pharmaceutical Manufacturing Handbook: Production and

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MEMBRANE-COATED ORAL EXTENDED RELEASE 1203<br />

release rate will be entered. Ragnarsson et al. [49] have shown that the solid material<br />

disappears earlier as the drug solubility increases <strong>and</strong> that the third stage with<br />

time - dependent <strong>and</strong> decreasing release rate appears earlier compared to drugs with<br />

lower solubility.<br />

The contribution of diffusion to the release process can be modeled by using<br />

Fick ’ s fi rst law. For diffusion of a substance through the membrane, it will turn out<br />

as (assuming sink conditions)<br />

dMt<br />

DmKmA D K AC<br />

= JA = ( Cs −Cb)=<br />

dt<br />

h<br />

h<br />

m m s (6)<br />

where K m is the partition coeffi cient for the drug between the membrane <strong>and</strong> solution,<br />

D m is the diffusion coeffi cient in the membrane, A is the area of the membrane,<br />

h is the thickness of the membrane, <strong>and</strong> C s <strong>and</strong> C b are the concentrations on the<br />

inside of the membrane surface <strong>and</strong> in the bulk, respectively. The equation for diffusion<br />

through pores or cracks resembles Equation (6) :<br />

dM<br />

JA<br />

dt<br />

DKA<br />

t ε<br />

DεKAC = = ( Cs −Cb)=<br />

hτ<br />

hτ<br />

s (7)<br />

where ε <strong>and</strong> τ are introduced to describe the porosity <strong>and</strong> tortuosity in the<br />

membrane, respectively. The parameters D m <strong>and</strong> K m in Equation (6) are replaced<br />

in Equation (7) by D <strong>and</strong> K , which are the diffusion coeffi cient in the solution<br />

inside the pores <strong>and</strong> the partition coeffi cient between the solution <strong>and</strong> materials<br />

surrounding the liquid - fi lled pores, respectively. Equations (6) <strong>and</strong> (7) depend on<br />

the concentration gradient over the membrane, <strong>and</strong> both are independent of the<br />

time.<br />

The osmotic contribution to the drug transport is described by the so - called<br />

Kedem – Katchalsky equations (based on nonequilibrium thermodynamics) [50, 51] .<br />

A simplifi ed version is<br />

dMt<br />

ACsLpσΔΠ = JA =<br />

(8)<br />

dt<br />

h<br />

where Δ Π is the osmotic pressure difference over the membrane <strong>and</strong> L p <strong>and</strong> σ are<br />

the hydraulic permeability <strong>and</strong> the refl ection, respectively.<br />

A comparison of Equations (6) – (8) shows important similarities; they depend on<br />

the solubility of the drug, the area of the device, <strong>and</strong> the thickness of the membrane.<br />

This means that an increased solubility, larger area of the membrane, <strong>and</strong> thinner<br />

membranes will facilitate the drug release rate. This can be exemplifi ed by a study<br />

by Ragnarsson <strong>and</strong> Johansson [11] , who showed that, for different salt forms of<br />

metoprolol, an increased solubility also increased the drug release rate, which was<br />

predicted from the equations. Furthermore, Equations (6) – (8) show constant <strong>and</strong><br />

time - independent release rates. This constant amount of released drug will be a<br />

biopharmaceutical benefi t since it theoretically makes it possible to achieve a constant<br />

concentration of the drug in the blood plasma.

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