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Technical Information
Preparation of Liposomes
1. Mechanism of Vesicle Formation
Liposomes (lipid vesicles) are formed when thin lipid films or lipid
cakes are hydrated and stacks of liquid crystalline bilayers become
fluid and swell. The hydrated lipid sheets detach during agitation
and self-close to form large, multilamellar vesicles (LMV) which prevents
interaction of water with the hydrocarbon core of the bilayer at the
edges. Once these particles have formed, reducing the size of the
particle requires energy input in the form of sonic energy (sonication)
or mechanical energy (extrusion).
2. Method of Liposome Preparation Properties of lipid formulations can vary depending on
the composition (cationic, anionic, neutral lipid species), however,
the same preparation method can be used for all lipid vesicles regardless
of composition. The general elements of the procedure involve preparation
of the lipid for hydration, hydration with agitation, and sizing
to a homogeneous distribution of vesicles. a. Preparation of lipid for hydration: When preparing
liposomes with mixed lipid composition, the lipids must first be
dissolved and mixed in an organic solvent to assure a homogeneous
mixture of lipids. Usually this process is carried out using chloroform
or chloroform:methanol mixtures. The intent is to obtain a clear
lipid solution for complete mixing of lipids. Typically lipid solutions
are prepared at 10-20mg lipid/ml organic solvent, although higher
concentrations may be used if the lipid solubility and mixing are
acceptable. Once the lipids are thoroughly mixed in the organic
solvent, the solvent is removed to yield a lipid film. For small
volumes of organic solvent (<1mL), the solvent may be evaporated
using a dry nitrogen or argon stream in a fume hood. For larger
volumes, the organic solvent should be removed by rotary evaporation
yielding a thin lipid film on the sides of a round bottom flask.
The lipid film is thoroughly dried to remove residual organic solvent
by placing the vial or flask on a vacuum pump overnight. If the
use of chloroform is objectionable, an alternative is to dissolve
the lipid(s) in tertiary butanol or cyclohexane. The lipid solution
is transferred to containers and frozen by placing the containers
on a block of dry ice or swirling the container in a dry ice-acetone
or alcohol (ethanol or methanol) bath. Care should be taken when
using the bath procedure that the container can withstand sudden
temperature changes without cracking. After freezing completely,
the frozen lipid cake is placed on a vacuum pump and lyophilized
until dry (1-3 days depending on volume). The thickness of the lipid
cake should be no more than the diameter of the container being
used for lyophilization.Dry lipid films or cakes can be removed
from the vacuum pump, the container close tightly and taped, and
stored frozen until ready to hydrate. b. Hydration of lipid film/cake: Hydration of the dry lipid
film/cake is accomplished simply by adding an aqueous medium to
the container of dry lipid and agitating. The temperature of the
hydrating medium should be above the gel-liquid crystal transition
temperature (Tc or Tm) of the lipid with the highest Tc before adding
to the dry lipid. After addition of the hydrating medium, the lipid
suspension should be maintained above the Tc during the hydration
period. For high transition lipids, this is easily accomplished
by transferring the lipid suspension to a round bottom flask and
placing the flask on a rotory evaporation system without a vacuum.
Spinning the round bottom flask in the warm water bath maintained
at a temperature above the Tc of the lipid suspension allows the
lipid to hydrate in its fluid phase with adequate agitation. Hydration
time may differ slightly among lipid species and structure, however,
a hydration time of 1 hour with vigorous shaking, mixing, or stirring
is highly recommended. It is also believed that allowing the vesicle
suspension to stand overnight (aging) prior to downsizing makes
the sizing process easier and improves the homogeneity of the size
distribution. Aging is not recommended for high transition lipids
as lipid hydrolysis increases with elevated temperatures. The hydration
medium is generally determined by the application of the lipid vesicles.
Suitable hydration media include distilled water, buffer solutions,
saline, and nonelectrolytes such as sugar solutions. Physiological
osmolality (290 mOsm/kg) is recommended for in vivo applications.
Generally accepted solutions with meet these conditions are 0.9%
saline, 5% dextrose, and 10% sucrose. During hydration some lipids
form complexes unique to their structure. Highly charged lipids
have been observed to form a viscous gel when hydrated with low
ionic strength solutions. The problem can be alleviated by addition
of salt or by downsizing the lipid suspension. Poorly hydrating
lipids such as phosphatidylethanolamine have a tendency to self
aggregate upon hydration. Lipid vesicles containing more than 60
mol% phosphatidylethanolamine form particles having a small
hydration layer surrounding the vesicle. As particles approach one
another there is no hydration repulsion to repel the approaching
particle and the two membranes fall into an energy well where they
adhere and form aggregates. The aggregates settle out of solution
as large floculates which will disperse on agitation but reform
upon sitting. The product of hydration is a large, multilamellar
vesicle (LMV) analogous in structure to an onion, with each lipid
bilayer separated by a water layer. The spacing between lipid layers
is dictated by composition with poly hydrating layers being closer
together than highly charged layers which separate based on electrostatic
repulsion. Once a stable, hydrated LMV suspension has been produced,
the particles can be downsized by a variety of techniques, including
sonication or extrusion. c. Sizing of lipid suspension:
i. Sonication*: Disruption
of LMV suspensions using sonic energy (sonication) typically produces
small, unilamellar vesicles (SUV) with diameters in the range of
15-50nm. The most common instrumentation for preparation of sonicated
particles are bath and probe tip sonicators. Cup-horn sonicators,
although less widely used, have successfully produced SUV. Probe
tip sonicators deliver high en-ergy input to the lipid suspension
but suffer from overheating of the lipid suspension causing degradation.
Sonication tips also tend to release titanium particles into the
lipid suspension which must be removed by centrifugation prior to
use. For these reasons, bath sonicators are the most widely used
instrumentation for preparation of SUV. Sonication of an LMV dispersion
is accomplished by placing a test tube containing the suspension
in a bath sonicator (or placing the tip of the sonicator in the
test tube) and sonicating for 5-10 minutes above the Tc of the lipid.
The lipid suspension should begin to clarify to yield a slightly
hazy transparent solution. The haze is due to light scattering induced
by residual large particles remaining in the suspension. These particles
can be removed by centrifugation to yield a clear suspension of
SUV. Mean size and distribution is influenced by composition and
concentration, temperature, sonication time and power, volume, and
sonicator tuning. Since it is nearly impossible to reproduce the
conditions of sonication, size variation between batches produced
at different times is not uncommon. Also, due to the high degree
of curvature of these membranes, SUV are inherently unstable and
will spontaneously fuse to form larger vesicles when stored below
their phase transition temperature.
ii. Extrusion**:
Lipid extrusion is a technique in which a lipid suspension is
forced through a polycarbonate filter with a defined pore size to
yield particles having a diameter near the pore size of the filter
used. Prior to extrusion through the final pore size, LMV suspensions
are disrupted either by several freeze-thaw cycles or by prefiltering
the suspension through a larger pore size (typically 0.2µm-1.0µm).
This method helps prevent the membranes from fouling and improves
the homogeneity of the size distribution of the final suspension.
As with all procedures for downsizing LMV dispersions, the extrusion
should be done at a temperature above the Tc of the lipid. Attempts
to extrude below the Tc will be unsuccessful as the membrane has
atendency to foul with rigid membranes which cannot pass through
the pores. Extrusion through filters with 100nm pores typically
yields large, unilamellar vesicles (LUV) with a mean diameter of
120-140nm. Mean particle size also depends on lipid composition
and is quite reproducible from batch to batch.
The three illustrations above are excerpted from
the book 'Liposomes in Gene Delivery' by Danilo D. Lasic, published
1997 by CRC Press LLC. Avanti thanks the publisher for kind permission
to reproduce these drawings.