preparation of porous polylactide microspheres by emulsion-solvent evaporation based on solution...
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POLYMERS FOR ADVANCED TECHNOLOGIES
Polym. Adv. Technol. 2005; 16: 622–627
Published online 24 June 2005 in Wiley InterScience (www.interscience.wiley.com). DOI: 10.1002/pat.629
Preparation of porous polylactide microspheres by
emulsion-solvent evaporation based on solution
induced phase separation
Yi Hong, Changyou Gao*, Yanchao Shi and Jiacong ShenDepartment of Polymer Science and Engineering, Zhejiang University, Hangzhou 310027, China
Received 9 December 2004; Revised 11 April 2005; Accepted 20 April 2005
Porous polylactide (PLA) microspheres were fabricated by an emulsion-solvent evaporation meth-
od based on solution induced phase separation. Scanning electron microscopy (SEM) observations
confirmed the porous structure of the microspheres with good connectivity. The pore size was in
the range of decade micrometers. Besides large cavities as similarly existed on non-porous micro-
spheres, small pores were found on surfaces of the porous microspheres. The apparent density of
the porous microspheres was much smaller than that of non-porous microspheres. Fabrication
conditions such as stirring rate, good solvent/non-solvent ratio, PLA concentration and dispersant
(polyvinyl alcohol, PVA) concentration had an important influence on both the particle size and
size distribution and the pore size within the microspheres. A larger pore size was achieved at a
slower stirring rate, lower good solvent/non-solvent ratio or lower PLA concentration due to longer
coalescence time. Copyright # 2005 John Wiley & Sons, Ltd.
KEYWORDS: polylactide; porous microspheres; phase separation; structure; density
INTRODUCTION
Polylactide (PLA) has been shown to be important serving as
tissue engineering scaffolds and drug delivery carriers
because of its good mechanical properties, non-toxicity, pro-
cessibility, and biodegradability. As a biomedical material,
PLA can be processed into solid products such as rods,1
bone screws,2 suture lines, drug carriers3 and microspheres,4
as well as porous structure such as scaffolds,5 non-woven fab-
rics6 and hollow microspheres.7 Among which the micro-
spheres are of particular interest because of their special
structure and tailorable properties. They have been, for
example, used as delivery vehicles for drugs, polypeptides,
proteins and genes.8–11 In the tissue engineering field, the
microspheres can also serve as microcarriers for cell
culture, having the unique feature that they can be directly
injected into the defect.12–14 Moreover, they can be further
assembled into a three-dimensional (3D) porous scaffold
either in vitro or in vivo to induce cell infiltration and tissue
regeneration.15
Some existing methods, such as phase separation,16
emulsion-solvent evaporation,9,10 spray drying17,18 have
been employed to prepare non-porous microspheres. Among
which the emulsion-solvent evaporation is frequently
adopted. In a typical procedure, a volatile organic phase
containing dissolved polymers is emulsified in an aqueous
phase at a continuous constant stirring rate. Then the volatile
solvent is evaporated gradually to form the spherical
polymer particles, which are generally non-porous inside.
However, microspheres with a porous structure in their
interior are much more appreciated than the non-porous ones
in many cases. For example, because of their large size and
low mass density, porous microspheres can be aerosolized
more easily than smaller non-porous microspheres, resulting
in higher respirable fractions of inhaled therapeutics. With
larger size, they can avoid phagocytic clearance from the
lungs before the therapeutic dose is delivered. These features
are particularly useful for controlled-release inhalation
therapy.19 However, dramatic reduction of acidic degrada-
tion products, mainly the lactic acid, can be achieved while
keeping the overall volume constant. This would be
extremely important for the spheres used as scaffolds in
tissue engineering, and injectable carriers in drug deliv-
ery.8,13,15 Concentrated acids surrounding the implant sites
will easily cause non-infected inflammation, and even tissue
necrosis. But few works have been reported on fabrication of
porous microspheres, which contain both tiny pores and
polymer matrix (the pore walls) throughout the sphere
bodies. Rapid solvent removal,20 porogen leaching12 and
double-emulsification19,21 have been used to fabricate porous
microspheres based on emulsion-solvent evaporation
method. Yet the procedures of these methods are rather
complicated for repeatable production and subtly operation.
Solution induced phase separation (SIPS) is a simple way to
obtain materials with porous structure. A typical system
contains polymers, good solvent and non-solvent. These two
kinds of solvents are miscible with each other. Along with an
Copyright # 2005 John Wiley & Sons, Ltd.
*Correspondence to: C. Gao, Department of Polymer Science andEngineering, Zhejiang University, Hangzhou 310027, China.E-mail: [email protected]
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increase of the non-solvent and the polymer concentration,
the polymer-rich phase will separate from the polymer-lean
phase. The porous structure is thus formed after removal of
the solvents. In principle, it is very similar to the traditional
emulsion-solvent evaporation process, except for the exis-
tence of the non-solvent. This feature makes the process
contain the simplicity, convenience and effectiveness of the
traditional emulsion-solvent evaporation, while porous
microsphere can be produced.
In this paper the fabrication of porous PLA microspheres
combining the methods of emulsion-solvent evaporation and
SIPS are reported. Scanning electron microscopy (SEM) is
employed to visualize the porous nature of the resultant
microspheres. The method introduced here could also be
extended to other soluble polymers. The fabricated porous
PLA microspheres may find diverse applications as drug
delivery carriers, tissue engineering scaffolds, cell carriers
and adsorption matrices, etc.
EXPERIMENTAL
MaterialsPLA (average Mw¼ 200 000) was synthesized according to
the method described previously.22 Methylene chloride
(CH2Cl2), n-hexane and poly(vinyl alcohol) 124 (PVA 124,
average Mw 85 000–124 000, 98–99% hydrolyzed) are all of
analytical grade and used as received.
Preparation of porous PLA microspheresIn a typical fabrication process, 0.5 g PLA was dissolved in
9 ml methylene chloride. Then 1 ml n-hexane was added
into the solution. The transparent 5% PLA/CH2Cl2-hexane
solution (oil phase) was poured into 100 ml water (water
phase) containing suitable amount of PVA dispersant. The
oil to water ratio was kept at 1:10. The system was stirred at
a constant rate for 24 hr at 258C to evaporate the organic sol-
vent. After collected by filtration and washed with deionized
water for five times at reduced pressure, the microspheres
were dried at 358C for 3 days. Detailed formulations are
described in Table 1. All the yields were higher than 85%.
Size distribution and number average diameterThe microspheres were sieved by a series of stainless steel
meshes and weighted. Number average diameter of the
microspheres was calculated according to eqn (1).
Dn ¼X DiWi=½4�ðDi=2Þ3�=3�
PWi=½4�ðDi=2Þ3�=3�
ð1Þ
where Dn represents number average diameter, Wi repre-
sents weight of the microspheres at i size, and Di represents
average diameter at i size. r represents the density of the
microspheres, which is regarded as a constant for the same
batch of products.
Apparent density of the porous microspheresA known volume (V) of the vessel was filled with the dried
porous microspheres and weighed (W, three parallel mea-
surements were taken). The apparent density (ra) was calcu-
lated according to eqn (2) under the hypothesis that the size of
the porous spheres was the same.
�a ¼W
V � Cð2Þ
where C, 0.601, is the theoretical value of a 3D loose random
packing density of spheres.23 Introduction of this constant
can make the apparent density closer to the real density
of the porous microsphere because the packing holes can
be ruled out.
Scanning electron microscopy (SEM)Scanning electron micrographs were taken on a JSM 5000
after being treated under reduced pressure for 3 days and
coated with gold. A cross-section of the microspheres was
fabricated by imbedding the microspheres in aqueous paraf-
fin. After complete solidification, the hardened paraffin was
then cut into pieces with a blade. Hemispheres imbedded in
the paraffin were extensively washed with n-hexane. The
average diameter of the inner pores was measured by SMILE
VIEW software supplied by JEOL Company.
RESULTS AND DISCUSSION
Scheme 1 presents the microstructure alteration in the fabri-
cation process of the porous PLA microsphere. In this system,
methylene chloride and n-hexane serve as a good solvent and
a non-solvent for PLA, respectively. They are also miscible
with each other. The PLA solution dissolved in the mixed
solvents is poured into a continuously stirred PVA aqueous
solution. The oil phase is subsequently dispersed into a
large number of small droplets under agitation. Though
both the organic solvents are volatile, the evaporation speed
of methylene chloride, however, is faster than that of n-hex-
ane because of its lower boiling point (40.48C). Therefore, the
ratio between methylene chloride and n-hexane will decrease
gradually along with the evaporation process, accompanying
Table 1. Properties of the porous microspheres as a function of fabrication conditionsa
SampleCPLA
(w/v)CPVA
(w/v)Stirring rate
(rpm)Solvent/
non-solventDn
(mm)Yield(%)
ra
(g/cm3)Inner pore
(mm)
A 5% 0.8% 300 9:1 471 98.5 0.263 24� 4B 5% 0.8% 500 9:1 290 98.7 0.356 16� 3C 5% 0.8% 800 9:1 176 97.3 0.386 12� 2D 5% 0.8% 500 9.5:0.5 251 86 0.475 5� 1E 5% 0.8% 500 8:2 413 87 0.213 30� 5F 5% 0.5% 500 9:1 390 99.7 0.306 10� 2G 3% 0.8% 500 9:1 241 99.2 0.246 20� 4H 8% 0.8% 500 9:1 429 87.9 0.395 7� 2
aOil/water ratio was 1:10 and evaporation temperature was 258C.
Copyright # 2005 John Wiley & Sons, Ltd. Polym. Adv. Technol. 2005; 16: 622–627
Preparation of porous polylactide microspheres 623
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with increase of the PLA concentration. When the PLA con-
centration and the good solvent/non-solvent ratio reach a cri-
tical point, phase separation will occur. Along with the
further solvent evaporation, the polymer-lean phase will
spread and coalesce, resulting in size increase of a single
phase which corresponds to the tiny pores after complete sol-
vent removal. Finally, the polymer-lean phase will form the
pores surrounded by the polymer matrix formed from the
polymer-rich phase. Apparently, the phase separation occurs
mainly in the droplets, hence has no or at least minimal influ-
ence on the fabrication process, and on other properties of the
resultant microspheres such as size and size distribution.
All the microspheres are spherical as shown in Fig. 1. The
porous PLA microspheres possessed a rough surface with
many cavities and small pores. By contrast, only large cavities
were observed on the microspheres without addition of
Solvent evaporation
Phase spreadin droplet
Complete solventevaporation
Polymer-lean phase
porous PLAmicrosphere
Pore
PVA aqueoussolution
PLA+CH2Cl2+Hexane
PLA solutiondroplet
Solvent evaporation
Phase separationin droplet
Polymerrich phase
Hexane/CH2Cl2 ratio
PLA concentration
Coalescence
Scheme 1. Illustration to show the preparation and microstructure alteration processes of
porous PLA microspheres.
(a) (b)
500µm 100µm
100µm
(c)
100µm
Figure 1. SEM images to show the surface morphologies of microspheres. (a)
Sample A, (b) sample A with higher magnification (see Table 1 for sample
designation), (c) non-porous microspheres.
624 Y. Hong et al.
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the non-solvent, n-hexane (Fig. 1c). No small pores could be
detected in this case. The other distinct difference is that the
porous microspheres float on water while the non-porous
microspheres sedimentate under water. The reason for the
formation of the big cavities is not quite clear at present.
Solvent evaporation could be basically ruled out since
evaporation at higher temperature (for example 608C) has
yielded porous microspheres with same surface morphol-
ogy. A possible reason could be that the shear stress
may create defects during the solvent evaporation process.
The small pores on the porous microspheres, however, are
attributed to the removal of the non-solvent, i.e. the polymer-
lean phase.
SEM observations reveal the porous structure in the
interiors of the PLA microspheres, as exemplified here with
three typical samples (Fig. 2). The irregular pores connect
with each other and homogenously distribute throughout the
whole spheres. This nice connecting other than close pore
structure would be favorable for loading of substances in the
case required. The inner pore size also was variable by
fabrication conditions as presented later. It is worth noting
that the paraffin imbedding is a very useful technique to
maintain the initial microstructure of the sliced micro-
spheres.
To explore the controlling factors for the microstructure of
the porous PLA microspheres, the polymer concentration,
the dispersant concentration, the stirring rate and the good
solvent/non-solvent ratio were varied as listed in Table 1.
Stirring rateKeeping other conditions constant, the influence of stirring
rate was firstly investigated with respect to particle size, par-
ticle size distribution, apparent density and inner pore size
(Table 1 sample A, B and C, Figs. 2 and 3). Along with the
increase in the stirring rate from 300 to 800 rpm, the number
average diameter of the particles was decreased from 470 to
180 mm, respectively (Table 1). All the particle size distribu-
tions were quite narrow and accordingly shifted to the smal-
ler size region (Fig. 3a–3c). By contrast, the apparent density
of the microspheres was increased accompanying with the
reduction of the inner pore size of the microspheres (Table 1
and Fig. 2).
At a higher stirring rate, a larger shear energy is supplied.
Hence larger surface area can be equilibrated, which
corresponds to smaller droplets and particle size.24 Theore-
tically, the apparent density can characterize the change of
porosity of the porous PLA microspheres, i.e. a lower density
should correspond to a higher porosity. From this point of
view, the porosity of the microspheres should decrease as a
function of the stirring rate, or the particle size. However this
is not definite since the porosity is theoretically decided by
the polymer concentration assuming that the extent of the
volume shrinkage is constant for all the systems during
solvent removal. The particle size and size distribution may
also influence the detection since the 3D loose random
packing density can be altered in practice, e.g. smaller than
the proposed value, 0.601. To testify this influence and to
compare the apparent density of porous particles with non-
porous ones, non-porous microspheres with diameters
ranging 100–154, 154–180, 280–450 and 450–710 mm were
similarly characterized, resulting in apparent densities of
1.124, 1.113, 1.083 and 1.049 g/cm3, respectively. These data
indeed demonstrated that the apparent density of the non-
porous spheres was much bigger than that of the porous ones,
(c)
500µm 50µm
50µm 50µm
(a) (b)
(d)
Figure 2. SEM images to show the inner microstructure of the porous
microspheres. (a) Sample A, (b) sample A with higher magnification, (c) sample
B, and (d) sample E.
Preparation of porous polylactide microspheres 625
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and decreased as a function of particle size as well. These
results reveal also that the packing density of the measured
spheres is smaller than 0.601. Therefore, it is not clear at
present the exact correlation between the stirring rate and the
porosity. From those results, however, one can still conclude
that the influence of the stirring rate on the porosity should be
minimal.
As to the microstructure inside the porous spheres, a
higher stirring rate resulted in smaller pore size as shown in
Fig. 2(b) and 2(c) and Table 1. This is understood as a result of
faster solvent evaporating speed since the size of the droplets
is smaller. In the phase separation process, a faster solvent
removal would mean that the phase has a shorter coalescence
time, thus limiting the formation of larger phase domains.
Good solvent/non-solvent ratioGood solvent/non-solvent ratio is another key factor control-
ling properties of the porous microspheres. As the ratio
decreases, the solubility of polymers shall decrease, leading
to an accelerated phase separation process. As a result, the
separated phase domains would have longer time to grow
and coalesce with each other, thus larger pore size can be pro-
duced. As expected, when the ratio of the good solvent/poor
solvent decreased from 9.5:0.5 to 8:2, the pore size increased
from 5 to 30 mm accordingly as shown in Fig. 2 and Table 1
(sample B, D and E). The microspheres are solidified at a
much earlier stage during the solvent evaporation process
at a higher poor solvent ratio, leading to a smaller shrinkage
extent of the oil droplets (the shrinkage of the oil droplets in
solvent evaporation should always occur in the emulsion-
solvent evaporation method). Therefore, a larger particle
size was yielded as shown in Fig. 3(d) and Table 1. This
will, of course generate a lower density or higher porosity
of the microspheres, as illustrated in Table 1.
PLA concentrationThe concentration of polymers in the mixed solvents has
shown a proportional relationship with the particle size
and the apparent density (Table 1, sample G, B and H). The
viscosity of the system shall be increased at a higher polymer
concentration, leading to the dispersion difficulty. Hence
larger oil droplets will be produced. As such one can predict
that a higher polymer concentration would generate a
similar effect with slower stirring rate with respect to
particle size. Considering the relationship between the
particle size and the apparent density, one can find that the
0
10
20
30
40
50
60
>710
µm
450-
710µ
m
280-
450µ
m
180-
280µ
m
154-
180µ
m0
10
20
30
40
50
60
70
450-
710µ
m
>710
µm
280-
450µ
m
180-
280µ
m
154-
180µ
m
0
10
20
30
40
50
>710µm
450-
710µm
280-
450µm
180-
280µm
154-
180µm
100-
154µm
Wei
ghtr
atio
(%)
0
10
20
30
40
50
60
70
>710
µm
450-
710µm
280-
450µm
180-
280µm
Wei
ghtr
atio
(%)
(a)
(c) (d)
(b)
Wei
ghtr
atio
(%)
Wei
ghtr
atio
(%)
Figure 3. Particle size distribution histograms of the porous microspheres. (a) Sample A, (b) sample B, (c) sample C, and (d)
sample E.
626 Y. Hong et al.
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polymer concentration has exactly the reverse effect with the
stirring rate. Therefore, the higher apparent density at a
higher polymer concentration is understood as a result of a
larger mass existing in the microspheres, which also means
a smaller porosity. Regarding the pore size, the PLA concen-
tration has shown a reverse effect with the good solvent/non-
solvent ratio. As shown in Table 1, the pore size decreased
from 20� 4 to 7� 2 mm when the PLA concentration was
improved from 3 to 8%. This should be mainly caused by
the viscosity increase, which slows down the coalescence
after phase separation.
PVA concentrationThe oil droplets formed under agitation are stabilized by the
dispersant added in the system, being the PVA in the present
case. Table 1 (samples B and F) shows that a higher PVA
concentration yielded a smaller particle size but larger appar-
ent density and pore size. It is well understood that a higher
concentration of dispersant is beneficial to decrease the inter-
facial energy of oil droplets, thus smaller droplets that cor-
respond to larger surface area can be formed. As discussed
earlier, the apparent density increase would not mean a por-
osity decrease in the present case. With higher PVA concen-
tration, diffusion of the organic solvents might become
harder. This will likely prolong the coarsening time, hence
a larger pore size is achieved.
CONCLUSIONS
In this study porous PLA microspheres have been success-
fully prepared by the emulsion-solvent evaporation method
based on solution induced phase separation. Their porous
nature inside the spheres is verified by SEM observations.
These irregular pores are in the range of decade micrometers.
They are well interconnected and homogeneously distributed
throughout the entire microspheres. The apparent density of
the porous microspheres, from 0.20 to 0.45 g/cm3, was much
smaller than that of the non-porous microspheres (>1 g/cm3).
A slower stirring rate, lower good solvent/non-solvent ratio
or lower PLA concentration is helpful to achieve larger pore
size. Together with dispersant concentration, the particle
size is modulated from 180 to 470mm. Moreover, these fabri-
cation factors can also influence the apparent density more or
less either by size variance or porosity alteration or both.
AcknowledgementsThis study is financially supported by the Natural Science
Foundation of China (Nos 20434030 and 90206006) and the
National Science Fund for Distinguished Young Scholars of
China (No. 50425311).
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