Yi Bao1, Masatoshi Maeki2,3, Akihiko Ishida2, Hirofumi Tani2, Manabu Tokeshi2. 1. Graduate School of Chemical Sciences and Engineering, Hokkaido University, Kita 13 Nishi 8, Kita-ku, Sapporo 060-8628, Japan. 2. Division of Applied Chemistry, Faculty of Engineering, Hokkaido University, Kita 13 Nishi 8, Kita-ku, Sapporo 060-8628, Japan. 3. JST PRESTO, 4-1-8 Honcho, Kawaguchi, Saitama 332-0012, Japan.
Abstract
The translation of nanoparticles (NPs) from laboratory to clinical settings is limited, which is not ideal. One of the reasons for this is that we currently have limited ability to precisely regulate various physicochemical parameters of nanoparticles. This has made it difficult to rapidly perform targeted screening of drug preparation conditions. In this study, we attempted to broaden the range of preparation conditions for particle size-modulated poly(lactic-co-glycolic-acid) (PLGA) NP to enhance their applicability for drug delivery systems (DDS). This was done using a variety of organic solvents and a glass-based microfluidic device. Furthermore, we compared the PDMS-based microfluidic device to the glass-based microfluidic device in terms of the possibility of a wider range of preparation conditions, especially the effect of different solvents on the size of the PLGA NPs. PLGA NPs with different sizes (sub-200 nm) were successfully prepared, and three different types of taxanes were employed for encapsulation. The drug-loaded NPs showed size-dependent cytotoxicity in cellular assays, regardless of the taxane drug used.
The translation of nanoparticles (NPs) from laboratory to clinical settings is limited, which is not ideal. One of the reasons for this is that we currently have limited ability to precisely regulate various physicochemical parameters of nanoparticles. This has made it difficult to rapidly perform targeted screening of drug preparation conditions. In this study, we attempted to broaden the range of preparation conditions for particle size-modulated poly(lactic-co-glycolic-acid) (PLGA) NP to enhance their applicability for drug delivery systems (DDS). This was done using a variety of organic solvents and a glass-based microfluidic device. Furthermore, we compared the PDMS-based microfluidic device to the glass-based microfluidic device in terms of the possibility of a wider range of preparation conditions, especially the effect of different solvents on the size of the PLGA NPs. PLGA NPs with different sizes (sub-200 nm) were successfully prepared, and three different types of taxanes were employed for encapsulation. The drug-loaded NPs showed size-dependent cytotoxicity in cellular assays, regardless of the taxane drug used.
The advent of nanoparticles (NPs) has
helped to successfully overcome
the inadequacies of conventional drug delivery systems (DDS); they
have proven to be powerful weapons against a wide range of diseases.[1,2] NPs have been used to overcome numerous treatment obstacles.[3,4] They have demonstrated improved permeability, bioavailability, drug
pharmacokinetics, stability in biological matrices, reduced adverse
effects, and other features when used for drug administration.[5−9] Poly(lactic-co-glycolic-acid) (PLGA) polymeric
NPs, in particular, are FDA-approved polymers and one of the most
extensively utilized polymers in the development of nanomedicines
because of their high structural integrity, tunable properties, and
versatility in surface functionalization and stability.[10−12] Different functionalized innovative PLGA NPs that can target fatal
cancer cells have been reported in various studies.[13−16] However, only a few formulations
have been transformed into clinical applications, and only a handful
have had a substantial impact. Part of the challenge lies in the complexity
of optimizing the NPs because the optimal NPs parameters (surface
charge, particle size, surface roughness, etc.) need to be determined
according to different disease types and lesion locations.[17] In other words, to obtain finely customized
DDS and tailored medications, there is still a long way to go.The size-dependent cellular uptake in different cell lines has
been widely demonstrated,[18−22] and this has greatly encouraged the advancement of size-targeted
therapeutic regimens via precise particle size modulation. Microfluidic
devices can precisely modulate minimal fluid volumes in microscale-controlled
channels to prepare particles with controlled sizes and great batch-to-batch
reproducibility.[23−30] Furthermore, microfluidic-based nanoprecipitation allows for the
use of expensive therapeutics in small volumes to screen different
experimental conditions and to develop optimal formulations of NP-based
nanomedicines. For the preparation of NPs using the nanoprecipitation
method, the solvent effect is a significant factor in controlling
the NP size and encapsulating hydrophobic drugs.[31] In particular, tetrahydrofuran (THF) is widely used as
a solvent to dissolve various hydrophobic materials. Therefore, in
the microfluidic-based nanoprecipitation method, the use of THF as
the solvent can expand NP design, including hydrophobic drug encapsulation
and modification of NPs with hydrophobic materials.[32−34]Polydimethylsiloxane
(PDMS) is one of the most widely used materials
in microfluidic devices.[17] However, due
to the restrictive nature of PDMS, it cannot be applied to a wide
range of organic reagents because of the swelling of the solvent.[35,36] Therefore, only few studies have focused on comparing the effect
of solvents on the preparation of PLGA NPs in microfluidic devices.
Understanding the effect of solvents, including THF, on PLGA NP size
is essential for the development of novel PLGA-based nanomedicines.In this study, we investigated the effects of organic solvents
on the size of PLGA-NPs using a glass-based microfluidic device. Using
the glass-based microfluidic device, it was possible to first evaluate
the PLGA NP production behavior in the microchannel. In addition,
to verify the feasibility of diverse drug encapsulation screens, we
employed three distinct forms of taxanes [paclitaxel (PTX), cabazitaxel
(CTX), and docetaxel (DTX)] as model drugs for encapsulation and evaluated
in vitro experimental results. The prepared NPs maintained good batch-to-batch
reproducibility and size-dependent cytotoxicities. The glass-based
microfluidic device enables rapid optimization and screening of more
favorable conditions for the preparation of NPs for DDS, accelerates
clinical drug screening, and has the potential to assist rapid transfer
to preclinical investigations.
Results and Discussion
Effect of the Flow Condition on the PLGA NP Size
Figure shows an illustration
and a photograph of the microfluidic device used for PLGA NP production.
The structure of the glass-based microfluidic device was based on
a previous study, and it was obtained from Shin-Etsu Chemical Co.,
Ltd.. Here, microfluidic channels are fabricated by the typical wet
etching method.[37,38] Briefly, 10% hydrofluoric acid
is employed to etch the glass substrate. After the wet etching process,
the glass substrate with a microchannel was aligned to a plain glass
substrate with holes. The aligned glass substrates were bonded by
thermal fusion bonding.
Figure 1
(a) Top view of the glass-based microfluidic
device. The depth
of the channel was 60 μm. The device was equipped with 20 baffle
sets; (b) microscopy image of the glass device. The scale bar represents
100 μm; (c) schematics of the PLGA-based NPs preparation using
the glass device. (d) Glass-based microfluidic device used in this
study.
(a) Top view of the glass-based microfluidic
device. The depth
of the channel was 60 μm. The device was equipped with 20 baffle
sets; (b) microscopy image of the glass device. The scale bar represents
100 μm; (c) schematics of the PLGA-based NPs preparation using
the glass device. (d) Glass-based microfluidic device used in this
study.To evaluate the NP size controllability of the
glass device, we
produced PLGA NPs using acetonitrile as the solvent.Figure a shows
the PLGA NP sizes produced at the total flow rate (TFR) of 50, 500,
and 1000 μL/min using a flow rate ratio (FRR; aqueous phase/organic
phase) of 3. The NP size decreased from 146 nm to 37 nm when the TFR
was increased from 50 to 1000 μL/min, and the NPs were able
to maintain a good polydispersity index (PDI) under all flow conditions
(Figure a). This was
attributed to the more rapid solvent exchange process described in
the previous work.[39] This result implies
that the glass device can tolerate a higher TFR and can prepare monodisperse
particles with high reproducibility in this flow rate range. As shown
in Figure b, the NPs
prepared with the glass device were larger than those obtained with
the PDMS device under the same flow conditions; this was due to the
difference in the microchannels caused by the device fabrication process
(Figure c). The solvent
exchange performance of the glass device was reduced compared to that
of the PDMS device due to its wide microchannel structure. Overall,
the results imply that the glass device can tolerate a higher TFR,
produce monodisperse NPs with high reproducibility, and can be applied
to produce NPs using other organic solvents.
Figure 2
(a) Effect of the flow
condition on PLGA NPs size in the glass
device. (b) Difference between NPs prepared by the glass and PDMS
microfluidic devices. (c) Comparison of the design of glass and PDMS
devices. The NPs were prepared by dissolving polymers in acetonitrile
at FRR 3. The standard deviations from the repeated preparation experiments
were more than 3 times. P-values: ***≤0.0001;
**≤0.001, *≤0.05. Effect of solvent properties on the
PLGA NP size.
(a) Effect of the flow
condition on PLGA NPs size in the glass
device. (b) Difference between NPs prepared by the glass and PDMS
microfluidic devices. (c) Comparison of the design of glass and PDMS
devices. The NPs were prepared by dissolving polymers in acetonitrile
at FRR 3. The standard deviations from the repeated preparation experiments
were more than 3 times. P-values: ***≤0.0001;
**≤0.001, *≤0.05. Effect of solvent properties on the
PLGA NP size.The properties of the organic solvent affect the
diffusion of the
organic and aqueous phases within the microchannel, thus causing a
variation in the solvent exchange time. In addition, solvent polarity
is a major factor in the nanoprecipitation method used to control
the NP size.[31,40,41] However, PDMS cannot use various solvents, particularly low-polarity
solvents, owing to the swelling of PDMS.[35] In contrast to the PDMS device, the glass device showed high chemical
resistance and could use low-polarity solvents. We conducted experiments
using acetonitrile (ACN), dimethyl sulfoxide (DMSO), dimethylformamide
(DMF), and THF, which are miscible with water. The important physicochemical
parameters of these solvents are listed in Table and are relevant for the discussion of the
experimental data.
Table 1
Properties of Organic Solvents
molecular formulas
viscosity at 25 °C (cap)
surface tension (N/m)
Hildebrand solubility parameter (MPa1/2)
polarity Index
ACN
C2H–N
0.34
28.7
24.3
5.8
DMSO
C2H6OS
1.97
42.9
26.7
7.2
DMF
C3H7NO
0.80
36.4
24.8
6.4
THF
C4H8O
0.46
27.1
18.5
4.0
Water
H2O
0.89
72
47.9
10.2
As shown in Figure , PLGA NP formation behavior using ACN and THF was
similar, and monodisperse
NPs were prepared at flow rates of 50 or 500 μL/min with good
reproducibility. However, DMF and DMSO could only achieve the formation
of monodispersed NPs at a low flow rate of 50 μL/min. Polydisperse
NPs were formed at a TFR of 500 μL/min. The solvent parameters
listed in Table were
related to the particle size formation. At low TFR, the NP sizes were
148 and 162 nm, respectively, when ACN and THF were used as solvents.
In contrast, when DMSO and DMF were used, the NP sizes were almost
60 nm. As shown in Table , THF showed the lowest viscosity, surface tension, polarity,
and Hildebrand solubility, and the solvent properties of ACN were
similar to these. In comparison with THF and ACN, DMF and DMSO showed
higher viscosity, surface tension, polarity, and Hildebrand solubility
parameters. This result agrees with previous reports where PLGA NPs
were prepared by nanoprecipitation.[31,39,42]
Figure 3
(a) Effect of the solvent properties on number-weighted
NP size
when the TFF is 50 or 500 μL/min; (b) PDI of prepared NPs; (c,d)
NP size distribution prepared by four kinds of solvents: ACN, DMSO,
DMF, and THF. Solid lines represent the size distribution of intensity,
while the dotted lines are numbers. The error bar represents the standard
deviations from repeated experiments (at least three times). ACN (acetonitrile),
DMSO (dimethyl sulfoxide), DMF (dimethylformamide), and THF (tetrahydrofuran).
(a) Effect of the solvent properties on number-weighted
NP size
when the TFF is 50 or 500 μL/min; (b) PDI of prepared NPs; (c,d)
NP size distribution prepared by four kinds of solvents: ACN, DMSO,
DMF, and THF. Solid lines represent the size distribution of intensity,
while the dotted lines are numbers. The error bar represents the standard
deviations from repeated experiments (at least three times). ACN (acetonitrile),
DMSO (dimethyl sulfoxide), DMF (dimethylformamide), and THF (tetrahydrofuran).In addition, at a high TFR, the low repeatability
or wide size
distribution was attributed to the high viscosity and high surface
tension of DMSO and DMF. As explained by the principle of the two-block
polymer NPs’ mechanism in microfluidic devices, the solvent
exchange time (mixing time) of the organic solvent with water is essential,[39] and the high viscosity, surface tension, and
polarity of the organic solvent would cause a slower solvent change
in the microchannel during the NP formation process, which results
in the formation of large-sized NPs or aggregates. From the fluid
dynamics in the microchannel and solvent properties, we considered
the difference in the PLGA formation behavior between the TFR of 50
and 500 μL/min conditions when DMSO and DMF were the solvents.
The polarity of solvents was rapidly increased by mixing with the
water, particularly the TFR of the 500 μL/min condition. Therefore,
some PLGA molecules were immediately self-assembled to form NPs and
formed small-sized NPs. However, other organic solvent properties
such as viscosity and surface tension affected the mixing efficiency
of the microfluidic device and formed the large-sized NPs. In contrast,
the mixing efficiency of the microfluidic device at 50 μL/min
was not enough to form small-sized NPs, and monodispersed large-sized
NPs were produced by the slow solvent dilution. Based on these results,
the screening range for size-modulated NPs preparation conditions
may be enlarged, especially for a broader range of solvents. This
will be resulting in a rapid and broad range of DDS screening and
a significant step forward in later clinical settings.
Encapsulation of Different Kinds of Anti-cancer Drugs
Three different taxanes (PTX, CTX, and DTX) were used as model drugs.
PTX and DTX are semisynthetic derivatives of 10-deacetylbaccatin-III.
The natural PTX precursor molecule can be extracted from the European
yew tree easily and sustainably. CTX, a novel second-generation taxane,
is a dimethyl derivative of DTX bearing methoxy groups in place of
the hydroxyl groups at the C-7 and C-10 positions.ACN or THF
was used as the solvent to prepare NPs with a concentration of 5 mg/mL
of polymer, and the concentration of the drug being encapsulated was
0.5 mg/mL (10% of polymer). Similar to PTX-encapsulated NPs, CTX-
and DTX-encapsulated NPs also decreased in size with increasing TFR,
and no effect of solvent type on NP size was observed (Figure a). The encapsulation efficacies
(EEs) of the three different drugs in the NPs are shown in Figure b. The EE of PTX
was higher than that of CTX and DTX, regardless of TFR conditions.
This can be attributed to PTX having the highest molecular weight.
For the same mass concentration, a higher molecular weight means a
lower amount of substance, and thus, less unencapsulation in the polymeric
NPs; this implies a higher EE. In addition, the higher hydrophobicity
of PTX compared with other drugs is one of the reasons for its higher
EE.
Figure 4
Difference of TFR or solvent on different kinds of drug-encapsulated
NPs. (a) NPs size of PLGA-based NPs encapsulate PTX/CTX/DTX by employing
ACN or THF as the solvent; (b) EE of drug-loaded NPs. The standard
deviations were calculated from repeated preparation experiments that
were more than three times higher. ACN (acetonitrile) and THF (tetrahydrofuran).
Effect of PLGA NP size on cytotoxicity.2
Difference of TFR or solvent on different kinds of drug-encapsulated
NPs. (a) NPs size of PLGA-based NPs encapsulate PTX/CTX/DTX by employing
ACN or THF as the solvent; (b) EE of drug-loaded NPs. The standard
deviations were calculated from repeated preparation experiments that
were more than three times higher. ACN (acetonitrile) and THF (tetrahydrofuran).
Effect of PLGA NP size on cytotoxicity.2Particles with different NP sizes were prepared
to confirm that
size-modulated NPs are useful for screening future DDS for clinical
use. We used THF as the solvent; however, THF is not appropriate for
the PDMS device. The NP size was modulated by varying only the TFR
(50 or 500 μL/min) and encapsulating different types of taxane
(PTX, CTX, and DTX) anticancer drugs. These three drugs have similar
mechanisms of action: binding to microtubule proteins and impairing
the natural dynamics of microtubules, leading to mitotic arrest and
apoptosis.[43−45]As shown in Figure , NPs encapsulated with the three different
types of anticancer drugs
showed NP size-dependent cell growth inhibition in HeLa cells after
24 h of incubation at drug concentrations ranging from 0.02 to 20
μg/mL. In HeLa cells incubated with PTX-loaded NPs, the cell
viability of those incubated with 62 nm NPs decreased from approximately
70% to approximately 36% with increasing PTX concentration, while
that of cells incubated with 163 nm NPs decreased from 82 to 45%.
The results for CTX-loaded NPs were similar to those for PTX; with
increasing CTX concentrations, the cell viability decreased from 58
to 32% with 34 nm NPs and from 68 to 55% with 148 nm NPs. For DTX-NPs,
the viability of HeLa cells incubated with 85 nm NPs decreased from
21 to 5%, while that with 154 nm NPs decreased from 47 to 38%. Overall,
smaller NPs showed greater cytotoxicity. It has been previously shown
that PLGA has a particle size effect on cellular uptake.[19,46,47] However, few studies focusing
on in vitro NP size effects using the NPs prepared by the same polymer
precursors. Our study fills this knowledge gap. Furthermore, our study
demonstrated the ability of the glass-based microfluidic device to
broaden the range of NPs preparation conditions, especially solvent
conditions, compared to those using PDMS devices. These results strongly
demonstrate the great potential of the glass-based microfluidic device
as a large-scale screening device for the preparation of NPs for DDS
and the establishment of a particle-size-controllable DDS.
Figure 5
NP size effect
on HeLa cell viability by incubated 24 h. (a) PTX-loaded
NPs; (b) CTX-loaded NPs; (c) DTX-loaded NPs. Standard deviations were
calculated from the repeated experiment more than three times. P-values: *≤0.05.
NP size effect
on HeLa cell viability by incubated 24 h. (a) PTX-loaded
NPs; (b) CTX-loaded NPs; (c) DTX-loaded NPs. Standard deviations were
calculated from the repeated experiment more than three times. P-values: *≤0.05.
Conclusions
In this study, we have explored the effect
of condition, mainly
for different organic solvents, for preparing size-modulated sub-200
nm PLGA NPs using a glass microfluidic device, without changing the
polymer precursors. We also demonstrated the NP production of taxane-based
anticancer drugs as model polymers and model pharmaceuticals. More
specifically, under the preparative conditions of this study, ACN
and THF were more suitable for preparing size-modulated NPs with narrower
particle size distributions. In addition, PTX had a higher EE than
CTX and DTX. Our results also showed the particle size impact of NPs
on HeLa cells, regardless of the type of drug used in the in vitro
studies. We believe that the glass-based microfluidic device will
serve as a powerful tool for effectively advancing drug screening
and enbling tailored therapeutics in the future.
Experimental Section
Materials
PLGA (50:50 ratio, Mw = 24000–38000
Da) and PEG-PLGA (average MnPEG = 2000
Da, average MnPLGA = 11500 Da) were obtained
from Sigma-Aldrich (St. Louis, MO, USA). PTX, COX, and DOX were purchased
from Tokyo Chemical Industry Ltd. (Tokyo, Japan). Acetonitrile (ACN),
dimethyl sulfoxide (DMSO), dimethylformamide (DMF), and tetrahydrofuran
(THF) were purchased from FUJIFILM Wako Pure Chemical Corporation
(Osaka, Japan).
Preparation of Polymeric NPs
A 5 mg/mL mixture of PLGA
and PEG-PLGA with a mass ratio of 1:1, and 0.5 mg/mL
of different kinds of anti-cancer drugs (10% of polymer) were dissolved
in an organic solvent. The syringes were connected to the microfluidic
device, and the organic solution was fed with ultrapure water into
the microfluidic device from two different inlets using syringe pumps
(LEGATO 210; KD Scientific Inc., Hollistion, MA, USA). The collected
solution was dialyzed overnight in ultrapure water through a membrane
bag (MWCO:12–14 kD; Spectrum Laboratories, Inc., Canada) to
remove the organic solvent. The sizes of the NPs were evaluated using
dynamic light scattering (DLS. Zetasizer nano ZS ZEN360; Malvern Instruments,
UK).
Determination of the Encapsulation Efficiency
The drug
content of the NPs was determined using HPLC (HITACHI, Japan). The
NP solution was freeze-dried to a powder, which was then dissolved
in ACN. For PTX and DTX, the mobile phase consisted of ACN and water
(50:50 v/v) and a reverse-phase column was used to maintain a temperature
of 30 °C. The flow rate was 1.2 mL/min, and the UV detection
wavelength was 227 nm. CTX was ACN: water = 58:42 (v/v), the flow
rate was 1.0 mL/min, and the UV detection wavelength was 228 nm.The HPLC was calibrated using a standard solution containing 5–100
μg/mL of the drug in CAN (Figure S1). The encapsulation efficiency (EE) can be determined by the ratio
of the amount of drug inside the sample solution to the amount of
drug used for NPs preparation (eq )
Cell Viability
Human cervical cancer HeLa cells were
grown in Dulbecco’s modified essential medium (DMEM, Sigma-Aldrich,
St. Louis, MO, USA) supplemented with 10% (v/v) fetal bovine serum
(FBS) and 1% penicillin–streptomycin. The cells were maintained
in a humidified atmosphere containing 5% CO2 at 37 °C
in an incubator.The cells were seeded in 96-well plates at
a density of 5000 cells/well. After the cells adhered to the wall
of the plate, NPs were added and incubated with at least three replicate
wells per group for a certain period. After incubation, cytotoxicity
was assayed by adding 10 μL of Cell Counting kit-8 (CCK-8, Dojindo,
Japan) solution. The plates were further incubated for 1 h before
measuring absorbance at 450 nm using a microplate reader (Infinite-M
Nano 200 Pro, TECAN, Switzerland). Equation was employed to determine cell viability.where Asample, Apositive, and Anegetive are the absorbance of the sample, positive control, and negative
control, respectively.
Statistical Analysis
The results are expressed as the
mean ± standard deviation and were analyzed using T-TEST to demonstrate
statistical differences. A predictive value (P) ≤ 0.05 was
statistically significant.