Liquisolid Technique for Enhancing Dissolution
Rate: A Review
A.D. Deshmukh*,
S.R. Wasankar, R.M. Burghate,
M.A. Ughade
Vidyabharti
College of Pharmacy, Camp Road, Amravati, Maharashtra, 444602
ABSTRACT:
The bioavailability of many poorly water-soluble drugs is limited by
their dissolution rates which are in turn controlled by the effective surface
area present for dissolution Therapeutic effectiveness of a drug depends upon
the bioavailability. Solubility is one of the important parameter to achieve
desired concentration of drug in systemic circulation for pharmacological
response to be shown. The enhancement of oral bioavailability of poorly water
soluble drugs remains one of the most challenging aspects of drug development.
A more recent technique, “Liquisolid
technology” or “powdered solution technology” has been applied to
prepare water-insoluble drugs into rapid-release solid dosage forms. The technique is based upon the dissolving
the insoluble drug in the nonvolatile solvent and admixture of drug loaded
solutions with appropriate carrier and coating materials to convert into
acceptably flowing and compressible powders.
KEYWORDS: Insoluble drug, bioavailability, Liquisolid technique
INTRODUCTION:(1-8)
When
a drug is administered perorally in a solid dosage
form such as tablet, capsule or suspension it must be released from the dosage
form and dissolved in the gastrointestinal fluids before it can be absorbed.
The bioavailability of many poorly water-soluble drugs is limited by their
dissolution rates which are in turn controlled by the surface area present for
dissolution. Two consecutive transport processes can be identified to describe
the oral absorption of drugs from solid dosage forms:
1. Dissolution of the drug in vivo to produce a solution
2. Transport of the dissolved drug
across the G.I. membrane.
Each
process can be characterized by a rate constant. If the rate of dissolution of
the drug is significantly slower than the rate of absorption, the dissolution
of drug becomes the rate-limiting step in the absorption process and the particle
size of drug is of great importance in the transport from the GI tract to the
site of action. Bioequivalence can be estimated under certain conditions, major
rate limiting step for class II and IV is dissolution. Most drugs are passively
absorbed and their rates of absorption are dependent upon the concentration
gradients in each case; by increasing the dissolution rate in the GI tract, the
absorption rate is increased so long as the dissolution rate is still the
limiting step. This commonly occurs for drugs with limited water solubility.
Several
methods such as salt formation, solubilization, co
solvency, complexation, solid dispersion and particle
size reduction have been introduced to increase dissolution rate and thereby
oral absorption and bioavailability of such drugs. There are some practical
limitations of the above mentioned techniques. To overcome some of the problems
of above mentioned techniques a new technique called “Liquisolid
Technique” has been introduced which consist of dissolving of water insoluble
drug in non volatile solvent prior to compression which is well converted in
free flowing powder by using suitable coating and carrier material which is
free flowing, non adhering, dry and readily compressible powder which can be
readily compressed with the help of different compressible carriers like
(Starch, cellulose and lactose etc.) and else coating materials like (Colloidal
silica and Talc etc.).
Because
of drug present in the liquid medicament as solubilized
or molecularly dispersed state, as the dissolution is enhanced due to increased
surface area as well as wetting area. Their by the Liquisolid
technique is applied for water insoluble drugs to enhance dissolution rate may
also increase bioavailability.
The structure of the plaque biofilm might restrict the penetration of antimicrobial
agents, while bacteria growing on a surface grow slowly and display a novel
phenotype, one consequence of which is a reduced sensitivity to inhibitors[8,
12, 14]. Plaque is natural and contributes (like the resident microflora of all other sites in the body) to the normal
development of the physiology and defenses of the host [9, 10, 11].
LIQUISOLID
TECHNOLOGY[3, 4]
The
concept of powdered solutions enables one to convert a liquid drug or poorly water-soluble
solid drug dissolved in a suitable non-volatile solvent into a dry,
non-adherent, freeflowing and readily compressible
powder by its simple admixture with selected carrier and coating materials. Inspite of formulating the drug in a tableted
or a encapsulated dosage form, it is held in solution thus enhancing its
release.
Definitions:
Liquid
medication includes
liquid lipophilic drugs and drug suspensions or
solutions of solid water insoluble drugs in suitable non-volatile solvent
systems.
Liquisolid systems refers to powdered forms of liquid
medications formulated by converting liquid lipophilic
drugs, or drug suspensions or solutions of water insoluble solid drugs in
suitable nonvolatile solvent systems, into dry, non-adherent, free-flowing and
readily compressible powder admixtures by blending with selected carrier and
coating materials.
Carrier
material refers
to a preferably porous material possessing sufficient absorption properties,
such as microcrystalline and amorphous cellulose, which contributes in liquid
absorption.
Coating
material refers
to a material possessing fine and highly adsorptive particles, such as various
types of silica, which contributes in covering the wet carrier particles and
displaying a dry looking powder by adsorbing any excess liquid.
MATERIALS REQUIRED FOR FORMULATION[9, 10]
Drugs: Which are poorly soluble or else
insoluble drugs in water. Non volatile solvent: They may be hydrophilic or lipophilic in nature based on selection of type of
Formulation like immediate or control release.
Some
of them are
·
Polyethylene glycol,
·
Propylene glycol,
· Tween 80, 20,
·
Span 80, 20,
·
Liquid Paraffin,
· Cremophore L etc.,
Carrier material: They are preferred to be
coarser granular for acceptable flow, Methyl cellulose, Ethyl cellulose, Starch
etc (Avicel PH 102, Avivel
PH 200, Starch 1500, Ethocel)
Coating material: Nano
meter sized silica mostly preferred, like Aerosil,
talc.
Disintegrants: Mostly Super Disintegrates
like Sodium starch glycolate and crosspovidone.
Etc.,
PREPARATION
OF LIQUISOLID COMPACTS[1,3,4]
The
technology involved in preparation of liquisolid
compacts is simple but novel. Drug is dissolved in non-volatile solvent to form
a solution or a suspension. Inert, preferably water-miscible organic solvent systems
with high boiling point such as propylene glycol, liquid polyethylene glycols,
or glycerine are best suitable as liquid vehicles.
The wet particles so formed are converted into dry particles by the addition of
coating material. With the liquisolid technology, a
liquid may be transformed into a free flowing, readily compressible and
apparently dry powder by simple physical blending with selected excipients named the carrier and coating material. The
liquid portion, which can be a liquid drug, a drug suspension or a drug
solution in suitable non-volatile liquid vehicles, is incorporated into the
porous carrier material. The liquisolid systems are
made into compacts by the addition of other tablet excipients
like disintegrants as shown in Fig 1.
Fig 1. Steps involved in the formulation of liquisolid technique.
Theoretical
considerations in powdered solution formulations:
Determination
of optimum amount of carrier and coating material to ensure proper flowabillity and other formulation properties is a daunting
task. Mathematical expressions for the calculation of amount of excipients needed for powdered solution formulation was
proposed by Liao. The various terms used in deriving various mathematical
expressions are as described as in Table
1.
Table 1.
Mathematical expressions and their terms.
SYMBOL |
DEFINITIONS |
WLiquid |
Weight of liquid medication |
WSolid |
Weight of carrier and coating material |
Q |
Weight of carrier powder material |
R |
Powder excipients ratio |
Lf |
Liquid loading factor |
Φ |
Flowable
liquid retention potential of the carrier powder |
V |
Total volume of liquid |
VΦ |
Total volume of liquid absorbed into carrier material |
Ρ |
Density of liquid |
V φ |
Total volume of liquid adsorbed into coating material |
Flowable liquid-retention potential (Φ value)
of a powder:
Absorption
of a liquid by a powder material occurs when the absorbate
molecules diffuse inside the absorbent and are eventually captured and held by
the powder particles within their bulk. In some cases, the liquid is not truly
absorbed, and instead of being dispersed throughout the interior of the solid,
the liquid molecules only cling to its available surface i.e., internal and
external. This process is known as adsorption. Sometimes, however, depending on
the sorbent properties, both of these processes may occur simultaneously. The
combined process is termed sorption. For instance, if a liquid is incorporated
into a material which has a porous surface and closely matted fibers in its
interior, e.g., cellulose, both absorption and adsorption takes place. The
liquid is initially absorbed in the interior of the particles captured by its
internal structure. After the saturation of this process, adsorption of the
liquid onto the internal and external surfaces of the porous carrier particles
occurs. This liquid retention capacity of the powder material can be generally
referred to as the total liquid-retention potential or “holding capacity” of
the sorbent. The flowable liquid-retention potential (Φ
value) of a powder material describes its ability to retain a specific amount
of liquid while maintaining good flow properties. The Φ value is defined
as the maximum weight of liquid, (W liquid) that can be retained per
unit weight of the sorbent, (W solid), yielding a mixture with
acceptable flowabillity.
W liquid
W solid
As
the flowable liquid-retention potential of the
carrier material is approached, the liquid is held entirely in the interior of
the particles. This maintains the surface of carrier material relatively dry,
thus yielding powders with acceptable flow properties. When the Φ value is
exceeded, the interior of particles become saturated, resulting in the
formation of a liquid layer on the available surface of carrier particles.
Mechanism
of powdered solutions:
Suppose
a liquid drug or drug solution having a total volume V is incorporated
into a carrier powder material. Depending on the holding capacity of the
material, a part of the liquid, say,
VΦ
is absorbed and retained in the interior of the carrier particles. This volume
is dependent on the flowable liquid retention
potential (Φ) of the carrier material. The remaining liquid, VL, is
uniformly distributed and adsorbed onto the internal and external surfaces of
the particles.
When
a coating material, having a very small particle size, large specific surface,
and high flowable liquid retention potential, like
silica, is added to such a mixture, its fine particles will cover the wet
carrier material retaining the excess liquid.
This helps in maintaining acceptable flow properties. The resultant
product is a dry, nonadherent, and free flowing
powder mixture. T If only a specific volume (VΦ) of liquid is incorporated
into the carrier material, the liquid would be absorbed in the interior of the
particles without significantly wetting their surface, and consequently, the
powder would be dry and free flowing. This portion of the liquid is represented
by VC. It depends on the flowable liquid retention
potential, Φ, and the quantity, Q, of the carrier material used. Since Wsolid = Q and Wliquid
= VΦρ, where ρ is the
density of the liquid incorporated into the carrier material, Eq (1) can be expressed as
Principle
of sufficient coating:
For
the coating to be sufficient to convert the wet surface of the carrier
particles to dry surface, the volume VL of the adsorbed liquid must be retained
by the coating particles while maintaining their free-flowing texture. The
volume VL must be equal to a volume VΦ, of the liquid which is a quantity,
q, of the coating particles can retain and yet maintain acceptable flowabillity, therefore
Eq.(1)
can be rewritten as
Vφ, represents the same characteristics of the coating material as
represented by VΦ, for the
carrier
material in Eq.,(3). Thus it can be concluded that
Where
φ is the flowable liquid retention
potential of the coating material. Thus, Vφ is
dependent on the flowable liquid retention potential,
φ, and quantity, q, of the coating material. Substituting the values of
VΦ (Eq., 3) and V φ (Eq., 5) in Eq., 4 we obtain
Above equation can be rearranged as
Excipient Ratio (R):
In
some cases, however, the dosage formulation may require a specific ratio of
carrier/ coating material in the final powder admixture. This ratio may be
termed the excipient ratio, R, and
written
For
such cases, Eqs.(6, 7, 8) can be modified to include
the excipient ratio, R. Combining Eqs.(6,
9) , and considering a predetermined quantity, Q, of the carrier material, we
obtain
Furthermore,
solving for Q and considering a predetermined volume V of liquid, Eq.(1.10)
will become
Accordingly,
combining Eqs. (6, 9) and considering a predetermined
quantity, q, of the coating material, one obtains
For a
predetermined volume V of drug solution Eq(1.12) can
be solved for q to give
Many
authors were successful in applying the above developed mathematical
expressions to calculate the optimum amounts of ingredients required to produce
liquid/powder admixtures possessing, with acceptable flow characteristics.
Evaluation
of liquisolid systems Flow behavior (1-2, 12-19)
The flowabillity of a powder is of critical importance in the
production of pharmaceutical dosage forms in order to reduce high dose
variations. Angle of repose, Carr’s index and Hausner’s
ratio are used in order to ensure the flow properties of the liquisolid systems.
Precompression studies of the prepared liquisolid powder systems
In
order to ensure the suitability of the selected excipients,
differential scanning calorimetry, X-ray diffraction,
and scanning electron microscope studies are performed. In addition, flowabillity studies are also carried out to select the
optimal formulae for compression. Prior to the compression of the formulations
into tablets.
Differential scanning calorimetry
(DSC)
This
is prerequisite to know if any possible interaction present between the excipients and the drug used in the formulation. The
characteristic peak in the DSC thermogram belongs to
drug is absent that indicates that the drug is present in molecularly dispersed
in this system.
X- Ray diffraction (XRD)
To
get justification that the drug is in the solubilized
state or converted into amorphous form because of disappearance of
characteristic peaks belongs to drug and their by appearance of peaks which
belongs to carrier is absorbed.
Scanning
electron microscopy (SEM)
To
study the morphological characteristics of the materials used and the
drug–carrier systems; Scanning Electron Microscopy (SEM) is applied.
In vitro dissolution studies
Works of many researchers revealed that
technique of liquisolid compacts could be a promising
alternative for formulation of water-insoluble drugs. This technique of liquisolid compacts has been successfully employed to
improve the in-vitro release of poorly water soluble drugs as the poorly
soluble antiepileptic drug carbamazepine drug release
was measured from liquisolid compacts and commercial
tablets. It was observed that drug release from liquisolid
compacts and that from commercial tablets is comparable. Hydrocortisone (Spireas S et al., 1998), prednisolone
(Spireas S et al., 1998), Hydrochlorothiazide (Khaled et al., 2001), piroxicam (Javadzadeh Y et al., 2008; Javadzadeh
Y et al., 2005; Rakshit P, 2007), Carbamazepine
(Tayel et al., 2008). (Saharan et al) etc. Also
several water insoluble drugs, namely, nifedipine, gemfibrozil, and ibuprofen, have exhibited higher
bioavailability in rats as compared to their commercial counterparts.
In-Vitro
release
profiles of drug from the preferred tablets were studied using dissolution
apparatus and compared with the formulated Liquisolid
tablet. Drug release, % drug dissolved can be calculated of both the
formulation results are estimated.
ADVANTAGES (1-4)
Number of water-insoluble solid drugs can be formulated into liquisolid systems.
·
Can be
applied to formulate liquid medications such as oily liquid drugs.
·
Better
availability of an orally administered water insoluble drug.
·
Lower production cost than that of soft
gelatin capsules.
·
Production
of liquisolid systems is similar to that of
conventional tablets.
·
Can be
used for formulation of liquid oily drugs.
·
Exhibits
enhanced in-vitro and in-vivo drug release as compared to commercial
counterparts, including soft gelatin capsule preparations.
·
Drug
release can be modified using suitable formulation ingredients.
·
Drug
can be molecularly dispersed in the formulation.
·
Capability
of industrial production is also possible.
·
Enhanced
bioavailability can be obtained as compared to conventional tablets.
DISADVANTAGES (4,22)
·
Not applicable for formulation of high dose insoluble drugs.
·
If more amount of carrier is added to produce free-flowing powder,
the tablet weight increases which is difficult to swallow.
·
Acceptable compression properties may not be achieved since during
compression liquid drug may be squeezed out of the liquisolid
tablet.
·
Introduction of this method on industrial scale and to overcome
the problems of mixing small quantities of viscous liquid solutions onto large
amounts of carrier material may not be feasible.
·
Requirement
of high solubility of drug in non-volatile liquid vehicles.
APPLICATIONS (1-4)
·
These
can be efficiently used for water insoluble solid drugs or liquid lipophilic drugs.
·
Sustained
release as well as rapid release of drugs which are water soluble drugs can be
obtained by the use of this technique.
·
Solubility
and dissolution enhancement can be achieved.
·
Designing
of controlled release tablets can be done using various polymers.
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Received on 01.04.2012
Modified on 06.05.2012
Accepted on 12.08.2012
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