PRESENTATION ON
KINETICS OF DRUG RELEASE
FROM THEORY OF MASS TRANSFER
1
Presented by
Vikas Aggarwal
M.Pharm (Ist sem)
Pharmaceutics
Matrix Type
 Also called as Monolith dissolution
controlled system.
 Controlled dissolution by:
1.Altering porosity of tablet.
2.Decreasing its wettebility.
3.Dissolving at slower rate.
 First order drug release.
 Drug release determined by
dissolution rate of polymer.
 Examples: Dimetane extencaps,
Dimetapp extentabs.
Soluble drug
Slowly dissolving matrix
Encapsulation
 Called as Coating dissolution
controlled system.
 Dissolution rate of coat depends
upon stability & thickness of coating.
 Masks colour,odour,taste,minimising
GI irritation.
 One of the microencapsulation
method is used.
 Examples: Ornade spansules,
Chlortrimeton Repetabs
3
Soluble drug
Slowly
dissolving or
erodible
coat
Diffusion
 Major process for absorption.
 No energy required.
 Drug molecules diffuse from a region of higher concentration to
lower concentration until equilibrium is attainded.
 Directly proportional to the concentration gradient across the
membrane.
4
Matrix Diffusion Types
 Rigid Matrix Diffusion
Materials used are insoluble plastics such as PVP & fatty
acids.
 Swellable Matrix Diffusion
1. Also called as Glassy hydrogels.Popular for sustaining
the release of highly water soluble drugs.
2. Materials used are hydrophilic gums.
Examples : Natural- Guar gum,Tragacanth.
Semisynthetic -HPMC,CMC,Xanthum gum.
Synthetic -Polyacrilamides.
Examples: Glucotrol XL, Procardia XL
5
Matrix system
Rate controlling
step:
Diffusion of dissolved
drug in matrix.
6
Higuchi Equation
Q = DE/T (2A.E Cs)Cs.t)1/2
Where ,
Q=amt of drug release per unit surface area at time t.
D=diffusion coefficient of drug in the release medium.
E=porosity of matrix.
Cs=solubility of drug in release medium.
T=tortuosity of matrix.
A=concentration of drug present in matrix per unit
volume.
7
Reservoir System
 Also called as Laminated matrix device.
 Hollow system containing an inner core surrounded in water
insoluble membrane.
 Polymer can be applied by coating or micro encapsulation.
 Rate controlling mechanism - partitioning into membrane with
subsequent release into surrounding fluid by diffusion.
 Commonly used polymers - HPC, ethyl cellulose & polyvinyl
acetate.
 Examples: Nico-400, Nitro-Bid
8
Reservoir System Rate controlling
steps :
Polymeric content in
coating, thickness of
coating, hardness of
microcapsule.
9
Dissolution & Diffusion Controlled
Release system
 Drug encased in a partially soluble
membrane.
 Pores are created due to dissolution
of parts of membrane.
 It permits entry of aqueous medium
into core & drug dissolution.
 Diffusion of dissolved drug out of
system.
 Ex- Ethyl cellulose & PVP mixture
dissolves in water & create pores of
insoluble ethyl cellulose membrane.
10
Insoluble
membrane
Pore created by
dissolution of soluble
fraction of
membrane
Entry of
dissolution
fluid
Drug
diffusion
FACTORS INFLUENCING DRUG RELEASE
1. Permeation-Depends on crystallinity,nature of polymer,its
degree of polymerization,presence of fillers and
plasticizers,matrix properties like
thickness,porosity,diffusion layer etc.
2. Diffusion-diffusion coefficient
3. Partition coeffficient-imp. when matrix contains drug
dissolved in polymer.
4. Solubility-imp when drug is not dissolved in polymer
matrix,rather dispersed.
5. Pharmaceutical manipulations-porosity,compression
pressure,coat thickness,plasticizer conc., polarity of coating
materials etc.
This is the one dimensional form of fick’s first law.
As long as we are at steady state,solutions to Fick’s first law
provides a completely adequate description of the diffusional
process.
When a drop of dye is placed in a beaker of water at constant
temp,the dye tends to diffuse throughout the water,eventually
giving the solution a uniform colour.Dye molecules can be
viewed as being in a state of continual random motion.As
such,each molecule can move in any direction with equal
probability.The reason that molecules diffuse away from their
source is that there are more dye molecules at the source than in
the bulk solution.Therefore more molecules can move away
from the source than towards the source.
In first case amt. in core changes but conc remains same inside
upto a particular time and undergoes dilution so that dC
becomes constt. So when concentrations are changing with
time,as in the case of above experiment,we may know dC/dX
at the beginning of experiment,but the mass flow will
continually be changing the conc. gradient.Therefore it is
necessary to introduce time as a variable.Eqn then becomes-
This equation is called Fick’s 2nd law of diffusion.
Interpretation from the equation-
Rate of change in conc. in volume element is proportional to
area of change of conc. gradient in that region of field.
Diffusion coefficient(D) is a measure of rate of drug movt.
J=[dC/dt]x=D[d²C/dX²]ᵼ
FACTORS INFLUENCING DIFFUSIVITY
 Temperature-Diffusion is a dynamic process.Movt of a molecule
in a particular build of matrix will take place based on enthalpy
of system.As the temp. is increased,D value increases.At higher
temp.,there will be a higher flux rate.
As per Arrhenius equation -
Or lnD=lnD₀‒Ed⁄RT
D₀=temp independent frequency factor i.e. all molecules are at rest
at 0⁰K
Ed=Energy of activation for polymer diffusion
 Molecular wt.-As molecular weight and mol. Volume related to
each other directly,because density is constt.As molecular wt
increases,there will be more amt of resistance to movt.
D=Dₒe¯ᴱᵈ/ᴿᵀ
D α (1/Mol. Wt)⅓
Factors continued……… Radius of particles .Particles are assumed to be
spherical,small and electrically neutral.We can find out the
diameter of particles and its diffusivity in any particular
media.
where Na=Avogadro’s no(no. of particles in any particular
system)
As radius increases ,diffusion decreases.
Ƞ=viscosity.As viscosity increases diffusion decreases
D=RT/Na(6πƞ)r
4 Drug solubility As diffusion depends on conc gradient, drug solubility in
penetrant becomes important and then drug release becomes dissolution
dependent for sparingly soluble drugs . This can be expressed by Noyes –
Whitney eqn
Where dC/dt = Amt of drug release per unit time
K= dissolution rate constant
Cs= Saturation solubility in solvent
C = Conc in solvent at time t.
K= DsA/Vlb
Therefore Noyes- Whitney Eqn becomes
where Ds=diffusion coeff. in solvent
V=vol of soln.
dC/dt= DsA/Vlb (Cs-C)
dC/dt= K(Cs-C)
Time
Amt
releasing
DRUG DIFFUSION THROUGH MICROPARTICLES
When drug diffusion through microparticles/microcapsules is
concerned,drug transport involves dissolution of permeating
drug in polymer and diffusion across the membrane.
J=(DKA.ΔC/lm)
ΔC=conc difference on either side of membrane
lm=membrane thickness
K=partition coefficient of drug towards polymer
DK=permeability coefficient(imaginary)
DK/lm=permeability when lm is not known
D/lm=permeability constant(actual)
In case of nanoparticles of size 100 nm say and coat thickness
about 2nm or < 1nm,lm is insignificant,so DK/lm=DK only
Si-Nang and Carler eqn for drug release
from microcapsules
 dC/dt= [DsAK/Vlm]
 Where A= internal surface area of coating.
 K= Porosity and tortuosity.
Mechanisms/ Mathematical models of
drug release
1. First order
ln Xt = ln Xo+Kt (Release proportional to amount of
drug remaining )
Systems that follow the model – Water soluble drugs in
porus metrix
2 Zero order
Ft= Kot (Release independent of drug conc)
Eg : Osmotic Systems, Transdermal systems
3 Higuchi eqn.
Ft= Kн t½
Eg :Diffusion matrix formulations
4 Khanna et al modified Noyes Whitney eqn. or
Hixson and Crowell’s cubic root low of dissolution
W0⅓-Wt⅓= Kaᵼ
Where Wo = Original mass of drug
Wt= mass of drug remaining to dissolve at time t.
aᵼ = surface wt fraction at time t
5 Korsmeyer-Peppas eqn.
Mᵼ/Mₒ = Ktᵈ
Where Mᵼ/Mₒ fraction mass of drug released at time t.
Eg Hydrating sytems, Eroding systems where D is not
constant, thereby giving anomalous diffusion .
For Non-Fickian or anomalous diffusion m>0.5, which is
usually found in swellable systems
APPLICATIONS OF DRUG RELEASE DATA
1. Quality control
2. Understanding physiochemical aspects of drug delivery
system.
3. Understanding the release mechanisms.
4. Predict behaviour of system in vivo.
However there are difficulties in modelling drug release
data as there is great diversity in the physical form of
microcapsules/microparticles with respect to
size,shape,arrangement of core and coat,properties of
core like difffusivity,partition coeffficient,properties of
coat like porosity,thickness,crystallinity,inertness etc.
Brahmankar D.M., Jaiswal Sunil B.
“Biopharmaceutics and Pharmacokinetics A
Treatise Pg 408, 409,432.
Robinson Joseph R., Lee Vincent H.L.
“Controlled drug delivery Fundamentals and
Applications Pg 97, 101, 105.
Chien Yie W. “Novel Drug Delivery
systems” Pg 45,47,58,62,64,67.
REFERENCES
applicationsofdrugreleasedata-130212133522-phpapp01

applicationsofdrugreleasedata-130212133522-phpapp01

  • 1.
    PRESENTATION ON KINETICS OFDRUG RELEASE FROM THEORY OF MASS TRANSFER 1 Presented by Vikas Aggarwal M.Pharm (Ist sem) Pharmaceutics
  • 2.
    Matrix Type  Alsocalled as Monolith dissolution controlled system.  Controlled dissolution by: 1.Altering porosity of tablet. 2.Decreasing its wettebility. 3.Dissolving at slower rate.  First order drug release.  Drug release determined by dissolution rate of polymer.  Examples: Dimetane extencaps, Dimetapp extentabs. Soluble drug Slowly dissolving matrix
  • 3.
    Encapsulation  Called asCoating dissolution controlled system.  Dissolution rate of coat depends upon stability & thickness of coating.  Masks colour,odour,taste,minimising GI irritation.  One of the microencapsulation method is used.  Examples: Ornade spansules, Chlortrimeton Repetabs 3 Soluble drug Slowly dissolving or erodible coat
  • 4.
    Diffusion  Major processfor absorption.  No energy required.  Drug molecules diffuse from a region of higher concentration to lower concentration until equilibrium is attainded.  Directly proportional to the concentration gradient across the membrane. 4
  • 5.
    Matrix Diffusion Types Rigid Matrix Diffusion Materials used are insoluble plastics such as PVP & fatty acids.  Swellable Matrix Diffusion 1. Also called as Glassy hydrogels.Popular for sustaining the release of highly water soluble drugs. 2. Materials used are hydrophilic gums. Examples : Natural- Guar gum,Tragacanth. Semisynthetic -HPMC,CMC,Xanthum gum. Synthetic -Polyacrilamides. Examples: Glucotrol XL, Procardia XL 5
  • 6.
    Matrix system Rate controlling step: Diffusionof dissolved drug in matrix. 6
  • 7.
    Higuchi Equation Q =DE/T (2A.E Cs)Cs.t)1/2 Where , Q=amt of drug release per unit surface area at time t. D=diffusion coefficient of drug in the release medium. E=porosity of matrix. Cs=solubility of drug in release medium. T=tortuosity of matrix. A=concentration of drug present in matrix per unit volume. 7
  • 8.
    Reservoir System  Alsocalled as Laminated matrix device.  Hollow system containing an inner core surrounded in water insoluble membrane.  Polymer can be applied by coating or micro encapsulation.  Rate controlling mechanism - partitioning into membrane with subsequent release into surrounding fluid by diffusion.  Commonly used polymers - HPC, ethyl cellulose & polyvinyl acetate.  Examples: Nico-400, Nitro-Bid 8
  • 9.
    Reservoir System Ratecontrolling steps : Polymeric content in coating, thickness of coating, hardness of microcapsule. 9
  • 10.
    Dissolution & DiffusionControlled Release system  Drug encased in a partially soluble membrane.  Pores are created due to dissolution of parts of membrane.  It permits entry of aqueous medium into core & drug dissolution.  Diffusion of dissolved drug out of system.  Ex- Ethyl cellulose & PVP mixture dissolves in water & create pores of insoluble ethyl cellulose membrane. 10 Insoluble membrane Pore created by dissolution of soluble fraction of membrane Entry of dissolution fluid Drug diffusion
  • 11.
    FACTORS INFLUENCING DRUGRELEASE 1. Permeation-Depends on crystallinity,nature of polymer,its degree of polymerization,presence of fillers and plasticizers,matrix properties like thickness,porosity,diffusion layer etc. 2. Diffusion-diffusion coefficient 3. Partition coeffficient-imp. when matrix contains drug dissolved in polymer. 4. Solubility-imp when drug is not dissolved in polymer matrix,rather dispersed. 5. Pharmaceutical manipulations-porosity,compression pressure,coat thickness,plasticizer conc., polarity of coating materials etc.
  • 13.
    This is theone dimensional form of fick’s first law. As long as we are at steady state,solutions to Fick’s first law provides a completely adequate description of the diffusional process. When a drop of dye is placed in a beaker of water at constant temp,the dye tends to diffuse throughout the water,eventually giving the solution a uniform colour.Dye molecules can be viewed as being in a state of continual random motion.As such,each molecule can move in any direction with equal probability.The reason that molecules diffuse away from their source is that there are more dye molecules at the source than in the bulk solution.Therefore more molecules can move away from the source than towards the source.
  • 14.
    In first caseamt. in core changes but conc remains same inside upto a particular time and undergoes dilution so that dC becomes constt. So when concentrations are changing with time,as in the case of above experiment,we may know dC/dX at the beginning of experiment,but the mass flow will continually be changing the conc. gradient.Therefore it is necessary to introduce time as a variable.Eqn then becomes- This equation is called Fick’s 2nd law of diffusion. Interpretation from the equation- Rate of change in conc. in volume element is proportional to area of change of conc. gradient in that region of field. Diffusion coefficient(D) is a measure of rate of drug movt. J=[dC/dt]x=D[d²C/dX²]ᵼ
  • 15.
    FACTORS INFLUENCING DIFFUSIVITY Temperature-Diffusion is a dynamic process.Movt of a molecule in a particular build of matrix will take place based on enthalpy of system.As the temp. is increased,D value increases.At higher temp.,there will be a higher flux rate. As per Arrhenius equation - Or lnD=lnD₀‒Ed⁄RT D₀=temp independent frequency factor i.e. all molecules are at rest at 0⁰K Ed=Energy of activation for polymer diffusion  Molecular wt.-As molecular weight and mol. Volume related to each other directly,because density is constt.As molecular wt increases,there will be more amt of resistance to movt. D=Dₒe¯ᴱᵈ/ᴿᵀ D α (1/Mol. Wt)⅓
  • 16.
    Factors continued……… Radiusof particles .Particles are assumed to be spherical,small and electrically neutral.We can find out the diameter of particles and its diffusivity in any particular media. where Na=Avogadro’s no(no. of particles in any particular system) As radius increases ,diffusion decreases. Ƞ=viscosity.As viscosity increases diffusion decreases D=RT/Na(6πƞ)r
  • 17.
    4 Drug solubilityAs diffusion depends on conc gradient, drug solubility in penetrant becomes important and then drug release becomes dissolution dependent for sparingly soluble drugs . This can be expressed by Noyes – Whitney eqn Where dC/dt = Amt of drug release per unit time K= dissolution rate constant Cs= Saturation solubility in solvent C = Conc in solvent at time t. K= DsA/Vlb Therefore Noyes- Whitney Eqn becomes where Ds=diffusion coeff. in solvent V=vol of soln. dC/dt= DsA/Vlb (Cs-C) dC/dt= K(Cs-C) Time Amt releasing
  • 18.
    DRUG DIFFUSION THROUGHMICROPARTICLES When drug diffusion through microparticles/microcapsules is concerned,drug transport involves dissolution of permeating drug in polymer and diffusion across the membrane. J=(DKA.ΔC/lm) ΔC=conc difference on either side of membrane lm=membrane thickness K=partition coefficient of drug towards polymer DK=permeability coefficient(imaginary) DK/lm=permeability when lm is not known D/lm=permeability constant(actual) In case of nanoparticles of size 100 nm say and coat thickness about 2nm or < 1nm,lm is insignificant,so DK/lm=DK only
  • 19.
    Si-Nang and Carlereqn for drug release from microcapsules  dC/dt= [DsAK/Vlm]  Where A= internal surface area of coating.  K= Porosity and tortuosity. Mechanisms/ Mathematical models of drug release 1. First order ln Xt = ln Xo+Kt (Release proportional to amount of drug remaining ) Systems that follow the model – Water soluble drugs in porus metrix
  • 20.
    2 Zero order Ft=Kot (Release independent of drug conc) Eg : Osmotic Systems, Transdermal systems 3 Higuchi eqn. Ft= Kн t½ Eg :Diffusion matrix formulations 4 Khanna et al modified Noyes Whitney eqn. or Hixson and Crowell’s cubic root low of dissolution W0⅓-Wt⅓= Kaᵼ Where Wo = Original mass of drug Wt= mass of drug remaining to dissolve at time t. aᵼ = surface wt fraction at time t
  • 21.
    5 Korsmeyer-Peppas eqn. Mᵼ/Mₒ= Ktᵈ Where Mᵼ/Mₒ fraction mass of drug released at time t. Eg Hydrating sytems, Eroding systems where D is not constant, thereby giving anomalous diffusion . For Non-Fickian or anomalous diffusion m>0.5, which is usually found in swellable systems
  • 22.
    APPLICATIONS OF DRUGRELEASE DATA 1. Quality control 2. Understanding physiochemical aspects of drug delivery system. 3. Understanding the release mechanisms. 4. Predict behaviour of system in vivo. However there are difficulties in modelling drug release data as there is great diversity in the physical form of microcapsules/microparticles with respect to size,shape,arrangement of core and coat,properties of core like difffusivity,partition coeffficient,properties of coat like porosity,thickness,crystallinity,inertness etc.
  • 23.
    Brahmankar D.M., JaiswalSunil B. “Biopharmaceutics and Pharmacokinetics A Treatise Pg 408, 409,432. Robinson Joseph R., Lee Vincent H.L. “Controlled drug delivery Fundamentals and Applications Pg 97, 101, 105. Chien Yie W. “Novel Drug Delivery systems” Pg 45,47,58,62,64,67. REFERENCES