Jan. '012
PAGE for PUBLICATION / FIELD [JPN] [ENG]
PAGE for COLLABORATION [JPN] [ENG]
CONTENTS of MEMORANDUM s
§1. Release of Drug from or through a Wax Matrix
System
I. Basic Release Properties of the
Wax Matrix System
II. Basic Properties of Release from
or through the Wax Matrix Layer
III. Basic Properties of Release through
the Wax Matrix Layer
IV. Genaralized Expression of the Release
Process for a Reservoir Device Tablet
V. Applicability of the Square-Root
Law Equation for Release from a Wax Matrix
Tablet
VI. Analysis and Prediction of the Entire
Release Process of the Wax Matrix Tablet
§2. Dissolution of Solid Dosage Form
I. Dissolution and Simulation Curves
for Log-Normal Particle-Size-Distributed
Model System
II. Equations for the Dissolution of
Nondisintegrating Tablet under the Sink Condition
III. Equations for the Dissolution
of a Nondisintegrating Single Component Tablet
under a Nonsink Condition
IV. Equation for the Non-sink Dissolution
of a Monodisperse System
V. New Form Equations for the Non-sink
Dissolution of a Monodisperse System
VI. Dissolution of Nondisintegrating
Single Component Tables under Non-sink Condition
VII. Effect of Shape on the Dissolution
of Nondisintegrating Single Component Tablet
under Non-sink Condition
§3. Changes of Surface Area in the Dissolution
Process of Crystalline Substances
I. Changes of Surface Area in the Dissolution
Process of Crystalline Substances
II. Dissolution and Simulation Curves
for Mixed Systems of Sieved Particles
III. Dissolution and Simulation curves
for Symmetrical Particle-Size Distributed
Model Systems
IV. Dissolution and Simulation Curves
Estimated from Changes of Surface Area and
Cube Root Law
V. Dissolution and Simulation Curves
for Log-Normal Particle-Size-Distributed
Model Systems
VI. Simulation of Dissolution of Crystalline
Particle
VII. Simulation of Dissolution of Crystalline
Particle. II.
§4. Physico-Chemical Properties of Glycyrrhiz
Acid in Aqueous Media
I. Surface-active Properties and Formation
of Molecular Aggregate
II. Effect on Flocculation-Deflocculation
Behavior of Suspensions of Sulfathiazole
and Graphite
III. Solubilizing Properties for Dyes
and Medicinal Substance
IV. Emulsification of Oleic Acid
V. Critical Micelle Concentration of
Mixed Solutions of Glycyrrhizin and Sodium
Cholate
VI. Determination of Critical Micell
Concentration of Sodium Cholate by Iodine
Method
VII. Emulsifying Ability of Glycyrrhizin
and Stability of the Emulsions
.
contents
§1. Release of Drug from or through a Wax Matrix
System
Yonezawa Y., Ishida S., Suzuki S., Sunada
H..
The wax matrix layer was prepared from
a physical mixture of wax powder and soluble
component
( When a wax matrix system is prepared
from melted granules, troublesome factors
such as coverage and thickness of
wax on the soluble component must be considered.)
To obtain basic properties, the wax matrix system was prepared from a
physical mixture.
A modifed Higuchi equation , derivation of the H-my equation
I. Basic Release Properties of the Wax Matrix
System
Chem. Pharm. Bull., 49(11), 1448 - 1451 (2001)
Release from the wax matrix tablet,
examination of release direction
The release rate constant obtained
as g/min1/2 changed with the release direction.
The release rate constant obtained
as g/cm2 min1/2 was almost the same.
It was suggested that the relrease
property was almost the same and
the wax matrix structure was uniform
independent of release surface or direction
in a fixed mixing ratio.
II. Basic Properties of Release from or through
the Wax Matrix Layer
Chem. Pharm. Bull., 50( 2), 220-224 (2002)
Release from or through the reservoir
device wax matrix tablet
Fundamentally, tortuosity can not be
expressed by some meaningful factors, and
is obtained as an experimental result.
However, the tortuosity should be defined
by the matrix structure, and the structure
should be concerned with the porosity (ε).
as a result obtained was the totoursity(τ) value is ( nearly ) equal to ε-2.
III. Basic Properties of Release through
the Wax Matrix Layer
Chem. Pharm. Bull., 50( 6), 814 - 817 (2002)
Release from the reservoir device wax
matrix tablet
m/So = (P/L) Cs t , P= D(ε/τ)
m : the relreased amount , So : the surface area of matrix layer , L
: the thickness of matrix layer ,
P: the penetration coefficient, D
: the diffusion coefficient , Cs:the solubility
τ:the totoursity, ε : the porpsity
in the matrix layer
the totoursity value is ( nearly
) equal to ε-2 was ascertained.
IV. Genaralized Expression of the Release
Process for a Reservoir Device Tablet
Chem. Pharm. Bull., 50( 9), 1219-1222 (2002)
in the case of the totoursity value
was ( nearly ) equal to ε-2 ,
then the equation could be rewritten
by using the porosity
mL/ε3 = D So Cs ( t -Tf )
m : the relreased amount , L :
the thickness of matrix layer , ε :
the porpsity in the matrix layer
So: the surface area of matrix layer , D
: the diffusion coefficient , Tf : the lag time
V. Applicability of Square-Root Time Law
Equation for Release from a Wax Matrix Tablet
Chem. Pharm. Bull., 51( 8), 904 - 908 (2003)
Applicability Higuchi equation was
examined.
The estimated applicability was confirmed
by the release measurements
The remaining amount of drug in
the matrix gradually decrease,
and is insufficient to satisfy
a derivation condition of Higuchi equation.
VI. Analysis and Prediction of the Entire
Release Process of the Wax Matrix Tablet
Chem. Pharm. Bull., 53( 8), 915 - 918 (2005)
Simulated release amount increase infinitely
when the Higuchi equation was applied.
The remaining amount of drug in the
matrix gradually decrease,
and is insufficient to satisfy a
derivation condition of Higuchi equation.
Higuchi equation was modified by taking
into account of the released amount of drug.
Modifcation of Higuchi's equation,
named as the H-my equation cf
For the commom case of εCs << A in the initial state.
Q(=m/So) = { P ( 2A - εCs) Cs t }1/2 was simplified as:
Q(=m/So) = ( 2PACs t )1/2 dQ/dt = ( PACs / 2t )1/2 , dm/dt = So ( P A Cs / 2 t )1/2
the A-value should be corrected
by using the released amount (m)
dm/dt = So { P(Mo- m) Cs / 2Vmt }1/2 A =
Mo/ Vm , M = Mo- m
-dM/dt = So ( PMCs / 2Vmt )1/2
( M/Mo )1/2 = 1 - So ( PCs t / 2VmMo )1/2
simulation m = Mo[ 1 - { 1 - So ( PCs t / 2VmMo )1/2 }2 ]
the release process simulated by using the
H-my equation fitted well with the mesured
.
contents
§2. Dissolution of Solid Dosage Form
Yonezawa Y., Shinohara I., Shirakura K., Kawase S.,
Sasaki M., Wada A., Jinde Y., Otsuka A.,
Sunada H..
Derivation of several dissolution equations
based on Hixson -Crowell equation
crystal habit
exact expression of Hixson-Crowell equation another derivation
optional initial amount within the
solubility; the z-law equation ,the Ln-z equation
I. Dissolution and Simulation Curves for
Log-Normal Particle-Size-Distributed Model
System
Chem. Pharm. Bull., 38(11), 3107- 3111 (1990)
II. Equations for the Dissolution of Nondisintegrating
Tablet under the Sink Condition
Chem. Pharm. Bull., 39( 3), 769 - 772 (1991)
III. Equations for the Dissolution of a Nondisintegrating
Single Component Tablet under a Nonsink Condition
Chem. Pharm. Bull., 39(12), 3355 - 3358 (1991)
IV. Equation for the Non-sink Dissolution
of a Monodisperse System
Chem. Pharm. Bull., 42( 2), 349 - 353 (1994)
Derivation of equation for dissolution
with optional amount of crystalline particle
within the solubility.
1) dissolution with any optional initial
amount (Mo) within the solubility (Ms), Mo/Ms-value is a value other than 1/3
the z-law equation: (M/Mo)z = 1 - z k Ssp Cs t , z = 1/3 - Mo/Ms
M ( = Mo - m) : the undissolved amount remainning in
the solution
k: the intrinsic dissolution rate constant,
Ssp : the specific surface area, Cs: the solubility
V. New Form Equations for the Non-sink Dissolution
of a Monodisperse System
Chem. Pharm. Bull., 43( 2), 304 - 310 (1995)
1) dissolution with the initial amount
(Mo) equal to 1/3 of the solubility (Ms), Mo/Ms-value is equal to 1/3
the Ln-z equation : ln(M/Mo) = - k Ssp Cs t
M (= Mo - m): the undissolved amount remainning in
the solution
k: the intrinsic dissolution rate constant,
Ssp: the specific surface area, Cs: the solubility
2) dissolution with any optional initial
amount around the solubility was examined
the Lg-z equation : (m/Mo)-1 = 1 + k Ssp Cs t
VI. Dissolution of Nondisintegrating Single
Component Tables under Non-sink Condition
Chem. Pharm. Bull., 43(11), 1961- 1965 (1995)
Applicability of the z-law equation
and the Ln-z equations for dissolution of
tablet were examined
VII. Effect of Shape on the Dissolution of
Nondisintegrating Single Component Tablet
under Non-sink Condition
Chem. Pharm. Bull., 44( 5), 1043 - 1048 (1996)
Effect of tablet shape was examined
using the z-law equation and the Ln-z equation
were examined
the z-law equation and the Ln-z equation
1. The Ln-z equation is useful to determine
the intrinsic dissolution rate constant for
dissolution of any optional initial amount
.
in the region Mo<Ms/3, the treated line gradully goes downward
from the Ln-z equation line
Mo = Ms/3, the treated line fitted well with
he Ln-z equation line
in the region Mo>Ms/3, the treated line gradully goes upward
from the Ln-z equation line
2. Once the intrinsic dissolution rate constant
of a substance has been determined in advance,
the dissolution process of the substance
with any optinal initial amount within solubility
can be approximately predicted.
3. Application for dissolution of multi-components
tablet
the dissolution process could be roughly
prospected when the volume fraction was introduced.
as the uniform weight of tablet can be
used , a hydrodynamic effect can be neglected
and
the effect of additives can be evaluated
4.
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contents
§3. Changes of Surface Area in the Dissolution
Process of Crystalline Substances
Yonezawa Y., Yamamoto A., Shinohara I., Otsuka
A., Sunada H..
I. Changes of Surface Area in the Dissolution
Process of Crystalline Substances
Chem. Pharm. Bull., 36 (7), 2557 - 2561 (1988)
II. Dissolution and Simulation Curves for
Mixed Systems of Sieved Particles
Chem. Pharm. Bull., 37 (2), 467 - 470 (1989)
III. Dissolution and Simulation curves for
Symmetrical Particle-Size Distributed Model
Systems
Chem. Pharm. Bull., 37 (5), 1362 - 1365 (1989)
Dissolution of modelized particle-size
distribution
dissolution process and estimation
of an apparent particle size to define it
IV. Dissolution and Simulation Curves Estimated
from Changes of Surface Area and Cube Root
Law
Chem. Pharm. Bull., 37 (7), 1889 - 1894 (1989)
Exact expression of Hixson-Crowell
equations
the Cube root law equation : (M/Mo)1/3 = 1 - (1/3)k Ssp Cs t
the Negative two-third law equation
: (M/Mo)-2/3 = 1+ (2/3)k Ssp Cs t
V. Dissolution and Simulation Curves for
Log-Normal Particle-Size-Distributed Model
Systems
Chem. Pharm. Bull., 38 (4), 1024 - 1026 (1990)
Dissolution of a generalized log-normal
particle-size-distributied particles
Prediction of a dissolution precess
VI. Simulation of Dissolution of Crystalline
Particle
J. Soc. Powder Tech., 27(9), 621-625 (1990)
VII.Simulation of Dissolution of Crystalline
Particle. II.
J. Soc. Powder Tech., 28(9), 567-571 (1990)
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contents
§4. Physico-Chemical Properties of Glycyrrhizic
Acid in Aqueous Media
Yonezawa Y., Iba K., Tatsumi T, Watanabe
J., Sunada H., Otsuka A., Nakagaki M..
1. Surface-active Properties and Formation
of Molecular Aggregate
YAKUGAKU ZASSHI, 96 (2), 203 - 208 (1976)
2. Effect on Flocculation-Deflocculation
Behavior of Suspensions of Sulfathiazole
and Graphite
J. Pharm. Sci., 67 (2), 151 - 154 (1978)
3. Solubilizing Properties for Dyes and Medicinal
Substance
YAKUGAKU ZASSHI, 101 (9), 829 - 835 (1981)
4. Emulsification of Oleic Acid
YAKUGAKU ZASSHI, 103 (2), 203 - 208 (1983)
Emulsifing ability
Estimation of the emulsified particle
size by means of a light absorption method.
5. Critical Micelle Concentration of Mixed
Solutions of Glycyrrhizin and Sodium Cholate
YAKUGAKU ZASSHI, 103 (10), 1085 - 1090 (1983)
6. Determination of Critical Micelle Concentration
of Sodium Cholate by Iodine Method
YAKUGAKU ZASSHI, 99 (2), 217 - 219 (1979)
Applicabiliyt of the iodine method
7. Emulsifying Ability of Glycyrrhizin and
Stability of the Emulsions
J. Jpn. Cosmet. Sci. Soc., 8 (1), 61 - 66 (1984)
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