Ming Pin Alan
Lim
a,
Wei Li
Lee
a,
Effendi
Widjaja
b and
Say Chye Joachim
Loo
*a
aSchool of Materials Science and Engineering, Nanyang Technological University, 50 Nanyang Avenue, 639798, Singapore. E-mail: joachimloo@ntu.edu.sg
bProcess Science and Modeling, Institute of Chemical and Engineering Sciences, 1 Pesek Road, Jurong Island, 627833, Singapore
First published on 11th February 2013
Current focus on particulate drug delivery entails the need for increased drug loading and sustained release of water soluble drugs. Commonly studied biodegradable polyesters, such as poly(lactide-co-glycolide) (PLGA) and poly(L-lactide) (PLLA), are lacking in terms of loading efficiency of these drugs and a stable encapsulation environment for proteins. While hydrogels could enable higher loading of hydrophilic drugs, they are limited in terms of controlled and sustained release. With this in mind, the aim was to develop microparticles with a hydrophilic drug-loaded hydrogel core encapsulated within a biodegradable polyester shell that can improve hydrophilic drug loading, while providing controlled and sustained release. Herein, we report a single step method of fabricating microparticles via a concurrent ionotropic gelation and solvent extraction. Microparticles fabricated possess a core–shell structure of alginate, encapsulated in a shell constructed of either PLGA or PLLA. The cross-sectional morphology of particles was evaluated via scanning electron microscopy, calcium alginate core dissolution, FT-IR microscopy and Raman mapping. The incorporation of alginate within PLGA or PLLA was shown to increase encapsulation efficiency of a model hydrophilic drug metoclopramide HCl (MCA). The findings showed that the shell served as a membrane in controlling the release of drugs. Such gel-core hydrophobic-shell microparticles thus allow for improved loading and release of water soluble drugs.
Several systems studied for drug delivery have been reported, including mesoporous nanoparticles like silica dioxide5–7 and layer by layer polymeric capsules that are capable of functional release behaviour triggered by environmental stimuli.8–11 However, fabrication of such systems requires multiple steps that are complex and thus extended production time.8 On the other hand, the use of biodegradable polyesters, such as poly(lactide-co-glycolide) (PLGA) and poly(L-lactide) (PLLA), was well studied due to their biodegradability and biocompatibility, and their ability to sustain release over a long period of time in vivo.12 Fabrication techniques of such polymer based drug delivery systems are also well established, which include emulsion solvent evaporation, nanoprecipitation and coacervation.4,13,14 However, these polyesters are unable to load hydrophilic drugs at higher encapsulation efficiencies due to their relative hydrophobicities.3 Burst release from such systems is also an issue, due to the localization of drugs on particulate surfaces or pores formed within the microparticles.15,16 Furthermore, emulsion-based solvent evaporation techniques commonly employed to produce hydrophilic drug-loaded microparticles exacerbate the leaching of these drugs into the aqueous continuous phase during fabrication, thus resulting in low drug encapsulation efficiency.17 In view of this, hydrogel-based drug delivery systems have been used, as they potentially allow for improved loading of hydrophilic drugs18 and are also favoured as a friendly environment for protein encapsulation.19 Examples of such hydrogel systems include alginate and chitosan, which can be physically gelled using multivalent ions such as Ca2+.20 However, sustained release from such systems is limited, due to susceptibility of these hydrogels to swell in water when immersed in an aqueous environment.21
Composite hydrogel–PLGA particulate systems were thus developed to provide sustained release and increased loading of hydrophilic drugs.22–24 These particulate systems feature gel particulates dispersed within an internal matrix23 or on the surface of PLGA microparticles.22 However, these techniques require the prefabrication of the hydrogel component in an additional step, requiring additional time and effort during fabrication.
In this study, we report on a single step based fabrication technique to produce alginate–PLGA microparticles (Alg–PLGA MP) and alginate–PLLA microparticles (Alg–PLLA MP) with a gel-core/hydrophobic polymer-shell. It was hypothesized that such a core–shell system would allow for higher encapsulation efficiencies of hydrophilic drugs, while providing controlled and sustained release. Drug-loaded microparticles of a core–shell structure were previously shown to have better control over drug release when compared to blended composite microparticles.25 As such, the release profiles can be tuned according to diffusion kinetics and degradation rates of the polymer used. In addition, the objectives include studying how certain key synthesis parameters would result in the formation of a core–shell structure, and the mechanisms leading to the formation of core–shell microparticles. Metoclopramide hydrochloride (MCA), a model hydrophilic drug, was used, and the release of this drug was compared between this core–shell particulate system against a pure system of calcium alginate (CaAlg) beads. As a therapeutic agent, MCA is used as an antiemetic and a gastroprokinetic agent for the treatment of nausea and gastric stasis. It is also used as a radiosensitizer/chemosensitizer for lung carcinoma treatment.26
Fabricated microparticles | Oil phase | Internal aqueous phase | External aqueous phase | |
---|---|---|---|---|
Polymer type | NaCl | CaCl2 | NaCl | |
Alg–PLGA MP | PLGA | 1.35 M | 50 mM | 0.6 M |
Alg–PLLA MP | PLLA | 1.35 M | 50 mM | 0.6 M |
MCA-loaded | PLGA | — | 50 mM | — |
Alg–PLGA MP | ||||
MCA-loaded | PLLA | — | 50 mM | — |
Alg–PLLA MP | ||||
MCA-loaded | PLGA | — | — | — |
Neat-PLGA MP | ||||
MCA-loaded | PLLA | — | — | — |
Neat-PLLA MP |
An overview schematic of the fabrication process is shown in Fig. 1. The alginate solution was first emulsified in the PLGA/DCM solution under magnetic stirring for the formation of the primary water-in-oil (W/O) emulsion. This W/O emulsion was then further dispersed into a 100 ml aqueous solution of 0.5% (w/v) PVA, 50 mM CaCl2 and 0.6 M NaCl to form a double water-oil-water (W/O/W) emulsion, with an overhead stirrer (Calframo BDC1850-220). The stirrer was operated at 400 rpm for 3 hours to concurrently initiate the extraction of DCM and ionotropic gelation of sodium alginate. The resultant microparticles were then recovered via centrifugation, rinsed with deionised water, lyophilized and then stored in a desiccator for characterization.
Fig. 1 Schematic for the fabrication of alginate-polymer core–shell microparticles. |
Monolithic MCA-loaded neat PLGA and PLLA microparticles were also fabricated as a reference to MCA-loaded Alg-polymer core–shell microparticles. Sodium alginate was not included in the preparation of the internal aqueous phase.
Spectral pre-processing, including the removal of spikes due to cosmic rays, was carried out before the collected Raman spectra were subjected to the band target entropy minimization (BTEM) algorithm analysis. The BTEM algorithm was used to reconstruct pure component spectral estimates.28,29 When the entire normalized pure component spectra of underlying constituents had been reconstructed, the relative contributions of each measured point of these signals were calculated by projecting them back onto the baseline corrected and normalized data set. The colour-coded scale represents the intensities of each component recovered as a score image, in which the summation of the intensities (colour-coded scale) of all components at each particular grid pixel is equal to unity. These score images are then used to show the spatial distribution and the semi-quantitative content for all observed components in the microparticles.
Actual |
drug |
loading % (w/w) = 100% × (mass of |
drug |
loaded/total polymer mass) |
Encapsulation efficiency (%) = 100% × (actual |
drug |
loading/theoretical drug loading) |
To calculate the actual drug loading of the microparticles, approximately 5 mg of microparticles were weighed and digested in 1 M NaOH by ultrasonication, for 10 min in an 80 °C water bath. The resultant solution was then neutralized with 1 M HCl and filtered. The drug concentration of the solution was measured using a reverse phase high performance liquid chromatography (HPLC) method, using the Agilent 1100 HPLC system with an XDB-C18 column. The analysis was done in gradient mode, with a varied proportion of 0.1% (v/v) trifluoroacetic acid and acetonitrile as the mobile phase. The amount of MCA was quantified using a detection wavelength of 309 nm at room temperature.
Release data were fitted with the Peppas equation i.e. the power law, defined by the below equation:
Mt/M∞ = ktn |
Fig. 2 SEM image (a) of a cross-sectioned alginate–PLGA particle, and (b) the same microparticle subjected to trisodium citrate treatment (length denoted by scale bar is 100 μm). |
Fig. 3a shows the respective IR spectra of the microparticle shell and the core, with the representative spectra of pure PLGA and CaAlg for comparison. The spectrum of the core was different from the shell, with the presence of a strong broad peak at around 3500–3000 cm−1 arising from the core. This is characteristic of the O–H stretching of repeat –COOH and –OH group units on the alginate polymer chain.32 In addition, a COO− stretching absorption peak was also observed at around 1608 cm−1 for the alginate core.32,33 The doublet peak observed between 1790 and 1720 cm−1 for the shell, on the other hand, is representative of the CO stretch of the lactide and glycolide groups arising from PLGA. In essence, the IR spectra of the core and the shell of the microparticle match with the reference spectra of alginate and PLGA, respectively. In Fig. 3b, Raman mapping of a cross-sectioned microparticle and its associated pure component BTEM spectra estimates are shown, indicating the localization of each polymeric component. The core of the cross-sectioned microparticle again proved consistent to be alginate, which can be visually distinguished from the surrounding PLGA shell. The use of trisodium citrate to dissolve the alginate gel core shows that the shell left behind consists of PLGA. This is in agreement with the IR analysis and thus it is concluded that the formed microparticle has core–shell morphology of alginate and PLGA, respectively.
Fig. 3 FT-IR spectra (a) of a typical alginate–PLGA microparticle, (b) optical image of a cross-sectioned alginate-PLGA microparticle, with the respective Raman mapping score images and BTEM components derived from the mapped enclosed rectangular area shown in the optical image. |
Similar to Alg–PLGA MP, Alg–PLLA MP exhibited a core–shell structure, as shown in Fig. 4a. Similarly, the alginate core was removed when cross-sectioned particles were immersed in citrate solution (Fig. 4b). This is in concordance with the Raman mapping analysis in Fig. 5, whereby the core and the shell were verified to be alginate and PLLA, respectively. Carbon was also detected, as the particles were mounted on carbon tape during Raman mapping.
Fig. 4 SEM image (a) of a cross-sectioned alginate–PLLA particle, and (b) the same microparticle subjected to trisodium citrate treatment (length denoted by scale bar is 100 μm). |
Fig. 5 Optical image of a cross-sectioned alginate–PLLA microparticle, with the respective Raman mapping score images and BTEM components derived from the mapped enclosed rectangular area shown in the optical image. |
Fig. 6 SEM image (a) of a cross sectioned metoclopramide HCl loaded alginate–PLGA particle, and (b) the same microparticle subjected to trisodium citrate treatment (length denoted by scale bar is 100 μm). |
Fig. 7 Optical image of a cross-sectioned alginate–PLGA microparticle loaded with metoclopramide HCl, with the respective Raman mapping score images and BTEM components derived from the mapped enclosed rectangular area shown in the optical image. |
Table 2 compares the encapsulation efficiency of MCA in PLGA and PLLA microparticles, fabricated with and without the inclusion of alginate. The encapsulation efficiency of MCA in Alg–PLGA MP and Alg–PLLA MP was almost double of neat PLGA and PLLA microparticles. This indicates that the incorporation of a hydrophilic polymer can significantly improve loading and encapsulation of water soluble drugs.
The release profiles for the Alg–PLGA MP, Alg–PLLA MP and CaAlg beads are shown in Fig. 8. Pure CaAlg beads showed a complete drug release within 6 hours, while both Alg–PLGA MP and Alg–PLLA MP exhibited a suppression of the initial burst release across the first 24 hours, followed by a sustained release of MCA up to 4 and 7 days, respectively. Alg–PLLA MP exhibited a more sustained release as compared to Alg–PLGA MP.
Fig. 8 Release profile of metoclopramide HCl from Alg–PLGA MP, Alg–PLLA MP vs. naked calcium alginate beads across 7 days (main plot), and a closeup of the initial 24 hours (inset). |
The values of the release exponent n and the correlation coefficient R2 after fitting with the power law are shown in Table 3. This higher value of n for Alg–PLGA MP as compared to Alg–PLLA MP further suggests that the difference in release behaviour is influenced by a difference in the type of polymer used. This further leads to inference that the choice of polymer constructed for the shell could influence drug release profile and kinetics.
Particle type | Release exponent n | Linear correlation coefficient R2 |
---|---|---|
Alg–PLGA MP | 0.8194 | 0.9686 |
Alg–PLLA MP | 0.5104 | 0.9911 |
Alginate-polymer microparticles were fabricated through a W/O/W double emulsion solvent evaporation based technique, as shown in Fig. 1. This first involves the formation of a primary W/O emulsion, by emulsifying an aqueous solution containing NaAlg and NaCl into an oil phase (i.e. PLGA dissolved in DCM). The W/O emulsion was then subsequently dispersed into an external water phase with PVA, CaCl2 and NaCl dissolved. To achieve a stable W/O/W double emulsion, two different surfactants were used to disperse the primary W/O emulsion and the secondary double emulsion droplets in the external water phase.34 In this case, a hydrophobic Span 80 surfactant and a hydrophilic PVA surfactant were selected respectively to achieve this purpose. This subsequently forms the secondary double emulsion, as depicted in Fig. 9, and initiates two concurrent processes resulting in the formation of the core–shell microparticle. One is the extraction of a DCM solvent from the double emulsion droplet, which resulted in the precipitation of PLGA, and leading to the formation of the PLGA shell. The second concurrent process is the ionotropic gelation of the aqueous NaAlg phase within the inner aqueous droplet. Alginate can be gelled, i.e. physically cross-linked in the presence of divalent ions such as Ca2+ to form CaAlg hydrogels.35 The influx of Ca2+ ions from the external water phase into the internal alginate phase in this process causes the gelation of the dissolved alginate. In this manner, microparticles with an alginate-PLGA core–shell structure can be formed via this single fabrication step, whereby the water insoluble CaAlg core is gelled in situ within the hardening PLGA shell.
Fig. 9 Principles of alginate–PLGA core shell microparticle formation. |
With the use of a double emulsion based solvent evaporation technique, changes to the formulation can be made to tailor the type of microparticle formed. For instance, the shell material of the microparticle can be varied by simply using a different polymer dissolved in a compatible solvent, which is in turn removed via a solvent extraction process. In this study, the fabrication of Alg–PLLA MP was achieved by simply dissolving PLLA instead of PLGA, for the oil phase polymer solution. Also, the loading of drugs can be done by dissolving the drugs either in the aqueous alginate phase or the oil (polymer) phase prior to emulsification. For instance, MCA was loaded prior to emulsification by dissolving the drug crystals in the alginate aqueous phase.
Given that the technique is based on the formation of a W/O/W double emulsion, the presence of large osmotic pressure differences between the two aqueous phases in the emulsion can effect a large movement of water between both phases. This has an effect on the emulsion stability, which can lead to the rupture of the DCM/PLGA oil layer, causing the double emulsion droplets to break.34 Preliminary studies showed that microparticles fabricated without NaCl dissolved in the internal aqueous phase resulted in a large number of broken microparticles fabricated, which indicates the likelihood of rupture of the double emulsion during fabrication (see ESI†). At the same time, the contents of the internal aqueous phase (i.e. alginate and MCA) can also leach into the external phase due to molecular migration.36 Leaching of alginate may result in an inconsistent gel core formation or formation of inhomogeneous alginate gel structures due to alginate partitioning effects seen in confined low volumes of alginate.37 To overcome these issues, NaCl, as an osmolyte, was therefore dissolved in both inner and outer water phases of the double emulsion. The intent was to regulate the osmotic pressure between both aqueous phases of the double emulsion, while at the same time, reduce alginate leaching.38,39 The use of NaCl in the external phase also acts as a non-gelling ion in increasing the homogeneity of the gel formed.40,41
Interestingly, when MCA was loaded into the microparticles, NaCl was no longer required in the formulation. Given that alginate can form strong complexes with poly-cations such as chitosan and poly-L-lysine,27 it is deduced that the dissolved MCA in drug-loaded formulations could also form a similar complex with alginate in the same way poly-cations do, possibly due to the presence of amine/amide groups in the drug. Such interactions could possibly slow down and disrupt the coupled diffusion of the sodium alginate polymer to the gelling front, resulting in a reduced partitioning rate of alginate and leading to the formation of a more homogeneous gel.40,41 At the same time, the hydration of MCA in the internal water phase may also have resulted in an increased osmotic pressure in the double emulsion.42 As such, this would reduce the alginate leaching and increase the retention of alginate within the double emulsion droplet. A drug like MCA can therefore replace NaCl, as an osmotic agent, to produce drug-loaded Alg–PLGA MP.
In terms of drug loading efficiency, an overall increased loading of MCA was observed for the core–shell MP as compared to the monolithic polymer particles. Given that the encapsulation efficiency is affected by the drug loss to the external phase in emulsion solvent evaporation methods,15 the presence of a hydrophilic polymer like alginate can better associate with water soluble drugs, as compared to a more hydrophobic PLGA. This would subsequently increase retention of drugs within the emulsion droplets and reduce out-flux of water soluble drugs during fabrication.
Compared to naked CaAlg beads that exhibited complete burst release within one day, both Alg–PLGA MP and Alg–PLLA MP demonstrated sustained release over 4 and 7 days respectively (Fig. 8). This reduced burst was due to the shell of the microparticles serving as a protective encapsulating envelope, which acts as a membrane to regulate the release of drugs. While hydrogels are known to release their contents rapidly,3,21 the enveloping PLGA or PLLA shell limits the rate of water influx and acts as a rate-limiting membrane for drug diffusion.
The use of a more crystalline and hydrophobic polymer as the shell such as PLLA can further reduce the release rate. This is apparent in the difference of release behaviour between Alg–PLGA MP and Alg–PLLA MP, whereby the latter exhibited a slower gradual release instead of the faster dual phase release exhibited by Alg–PLGA MP. Also, by fitting the release data with the power law, a lower n exponent value for Alg–PLLA MP was obtained, as compared to Alg–PLGA MP. This difference suggests that the semi-crystallinity of PLLA retards the release of drug, as compared to the amorphous PLGA with a more open polymer network.43 With the above observations, it is hence envisaged that release kinetics of these core–shell microparticles can be regulated and tailored through appropriate selection of a polymer as the shell material.
With improved drug loading and the reduced burst release from core–shell alginate–PLGA/PLLA microparticles as compared to CaAlg, these findings would pave the way towards protein encapsulation using the same particulate architecture. Future work would entail investigation into the release behaviour and bioactivity of proteins from such microparticles. As such, this new particulate drug delivery platform would be beneficial in areas such as vaccines or peptide delivery.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c3bm00175j |
This journal is © The Royal Society of Chemistry 2013 |