Jinshan Guoab,
Dongfang Zhoua,
Jianqing Hubc,
Xuesi Chena,
Xiabin Jinga and
Yubin Huang*a
aState Key Laboratory of Polymer Physics and Chemistry, Changchun Institute of Applied Chemistry, Chinese Academy of Sciences, Changchun 130022, People's Republic of China. E-mail: ybhuang@ciac.ac.cn; Fax: +86 431 8526 2769; Tel: +86 431 8526 2769
bDepartment of Biomedical engineering, The Pennsylvania State University, W337 Millennium Science Complex, University Park, PA 16802, USA
cSchool of Chemistry and Chemical Engineering, South China University of Technology, Guangzhou 510640, China
First published on 16th April 2014
Click chemistry plays a dual role in emulsion microsphere (MS) preparation as both an in situ cross-linking method and a bioconjugation route. The morphology/shape of the MSs can be adjusted by applying surface click cross-linking and a porogen simultaneously. The emulsion click cross-linked MSs have potential application in drug delivery, and the preserved azide groups could be used for further surface conjugation with bioactive molecules.
First, alkyne and azide functionalized poly(γ-benzyl-L-glutamate) (PBLG), abbreviated as PBALG and PBN3LG, respectively, were synthesized by ester exchange reactions between PBLG and propargyl alcohol (for PBALG) or 3-azidopropanol (for PBN3LG) (Scheme 1), according to our previous work.22
Equal weights of PBALG and PBN3LG were mixed (the molar content of azide was higher than that of alkyne) and dissolved in an organic solvent (mixture of 1,2-dichloroethane and dimethylacetamide (DMAc)) to form an oil phase. An O/W emulsion was prepared under shear force using the oil phase and a polyvinyl alcohol (PVA) solution. After adding a copper catalyst (CuSO4-L-ascorbic acid sodium salt (NaLAc)) to the water phase, in situ emulsion surface CuAAC was promoted to form in situ emulsion click cross-linked and azide-functionalized poly(L-glutamate) microspheres (iECC-PLG-N3 MSs) (Scheme 2). The remaining azide groups were used for further surface conjugation of targeting units or fluorescent probes. A porogen was also used, and the co-effect of the porogen and emulsion surface click cross-linking on the morphology/shape of the microspheres was investigated by adjusting the copper catalyst concentration in the water phase and the polymer and porogen concentration in the oil phase (Table 1). The results are shown in Fig. 1.
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| Scheme 2 Preparation of azide-functionalized poly(L-glutamate) microspheres (iECC-PLG-N3 MSs) by in situ emulsion click cross-linking of an equal-weight mixture of PBALG and PBN3LG using CuAAC. | ||
| Samples | Polymer in oil phase content %(w/v) | Porogen to polymer ratio (mL g−1) | Catalyst to alkyne group ratio |
|---|---|---|---|
| 1 | 2 | 0 | 0 |
| 2 | 2 | 1 | 0 |
| 3 | 5 | 0 | CuSO4 (1.0 eq.), NaLAc (1.0 eq.) |
| 4 | 2 | 1 | CuSO4 (1.0 eq.), NaLAc (1.0 eq.) |
| 5 | 5 | 1 | CuSO4 (1.0 eq.), NaLAc (1.0 eq.) |
| 6 | 2 | 1 | CuSO4 (0.1 eq.), NaLAc (1.0 eq.) |
It can be seen that without a porogen and surface cross-linking, the obtained microspheres had an ordinary round shape with an average diameter around 10 μm (sample 1, Fig. 1A). After applying the porogen (decahydronaphthalene), but no copper catalyst, the obtained microspheres were also round shaped, but with a bigger diameter (around 20 μm) and possessed a lot of pores (sample 2, Fig. 1B). When no porogen but a copper catalyst was used, the obtained MSs were as nonporous as sample 1 (sample 3, Fig. 1C). Since the solvent was homogeneously dispersed in all microspheres, even after surface cross-linking, it was evaporated easily. When the porogen and the copper catalyst were applied simultaneously, the pores formed by the porogen decreased, some even disappeared. Changing the concentrations of the copper catalyst in the water phase and the polymer in the oil phase had a great effect on the morphology/shape of the obtained microspheres. When the polymer concentration in the oil phase was 2% (w/v), the porogen was 1 mL g−1 polymer, and the copper catalyst to alkyne group ratio was 1/1, the pores were almost sealed by surface click cross-linking. The obtained microspheres were non-porous spheres with a diameter typically of 5–10 μm (sample 4, Fig. 1D). When the polymer concentration in the oil phase was increased from 2% (w/v) to 5% (w/v), the shape of the obtained microspheres changed into a tetrahedron with all surfaces collapsed into the center, and the size of the microparticles also increased to around 15 μm (sample 5, Fig. 1E). It was found that, along with the increase of the polymer content in the oil phase, the size of the microspheres increased accordingly, which resulted in an overall increase of solvent and porogen encapsulated into each microparticle, because the ratio between the porogen and the polymer was kept at 1 mL g−1. Along with the fast evaporation of the organic solvent, followed by the slower evaporation of the gathered big porogen liquid drops, the surfaces of the microparticles collapsed resulting in the tetrahedral shape. Since the surface cross-linking speed was fast enough, nearly all pores were sealed (Fig. 1D). When the polymer concentration in the oil phase was kept at 2% (w/v), but the copper catalyst to alkyne group ratio decreased from 1/1 to 1/10, the obtained microparticles changed into wrinkled spheres with some small holes (sample 6, Fig. 1F). This walnut kernel-like morphology may be caused by the abatement of the surface cross-linking. The slow surface cross-linking could not seal the holes left by the solvent and porogen evaporation, and the thinner cross-linked shells collapsed and shrunk after solvent and porogen evaporation.
Emulsion clicked microspheres can be used as cross-linked drug carriers, which may improve drug loading efficiency and reduce the initial burst release, as reported before.5,6 The emulsion click method can adjust the morphology/shape23 of the microspheres or microparticles (Scheme 3A), which has been reported to be an important design parameter in drug delivery.24,25
Since the azide group content is higher than that of the alkyne group in the mixed polymer, some azide groups were preserved after surface cross-linking, which is shown in the FTIR spectrum of the iECC-PLG-N3 MSs (around 2100 cm−1 in Fig. 2). The residual azide groups could be used for further conjugation (Scheme 3B). As an example, a red fluorescent probe, alkyne-functionalized Rhodamine B,17 was conjugated onto the surface of the iECC-PLG-N3 MSs. The fluorescence microscopy image (Fig. 3A, from sample 4) clearly shows the red fluorescence covering the MS surface, which also proved the reactivity of the azide groups on the MS surface, implying the practicability of the surface modification on the iECC-PLG-N3 MSs by the click reaction. To further prove the pore interconnectivity of the porous MSs (sample 3) and detect the difference between porous MSs and nonporous MSs, fluorescence images of the cross-sections of Rhodamine B labeled porous and nonporous MSs were taken by confocal laser scanning microscopy (CLSM) using Z-section and measurement. The CLSM images show that most of the cross-section of the Rhodamine B labeled porous MS exhibits red fluorescence (Fig. 3B). As for the nonporous MS, only a red ring is observed (Fig. 3C, sample 4). These results further confirmed the interconnectivity of the formed pores, which enabled the permeation of the alkyne functional fluorescent dye, to conduct click reaction with the azide groups on the surface of the MSs in the process of surface conjugation.
To investigate if emulsion surface click cross-linking can improve the drug loading efficiency and reduce the initial burst release, BSA was chosen as a model for the drug loading and release research. The click cross-linked MSs possess a higher drug loading efficiency. The BSA encapsulation percentage was determined to be about 64.5% with a drug loading capacity around 19.6%. BSA loaded non cross-linked MSs (using no copper catalyst) were also prepared as a control, the BSA encapsulation percentage was around 42.4%, and the drug loading capacity was about 13.8%. From Fig. 4, it can be seen that after applying surface click cross-linking, the BSA release speed decreased, and the total release amount of BSA in 7 days was also much lower than that of BSA released from non cross-linked MSs, which agrees with the previous report.5
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| Fig. 4 BSA standard curve (A) and the accumulated release of BSA from non cross-linked and click cross-linked MSs. | ||
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1, the polymer concentration in the oil phase is 2% (w/v)), and 0.1 mL decahydronaphthalene (as porogen) was then added to the solution. The solution was dispersed in 1.0 wt% of a poly(vinyl alcohol) (PVA) solution (100 mL) by a high-shear dispersing emulsifier at a speed of 2000 rpm for 2–3 min. Then the O/W emulsion was poured into another 400 mL of PVA solution (1.0 wt%), which contained CuSO4 (1.0 eq. to alkyne group). After stirring for 1–2 min, NaLAc (1.0 eq. to alkyne group) was added to the system, and the mixture was stirred at 40 °C for 12–24 h to evaporate the solvent. After that, the microspheres were collected by centrifugation and washed several times with water and hot water, and then freeze-dried. iECC-PLG-N3 MSs with different polymer concentrations in the oil phase, porogen contents, as well as CuAAC catalyst system (CuSO4–NaLAc) contents (shown in Fig. 1C–E) were prepared. Non cross-linked microspheres made from an equal-weight mixture of PBALG and PBN3LG with or without the porogen (A and B in Fig. 1) were also prepared with the same method but without adding the CuAAC catalyst. Cross-linked microspheres without the porogen were also prepared as a control. The microspheres were characterized using a SEM and FTIR.
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1) to form the W/O emulsion. The W/O emulsion was then dispersed in 100 mL 1.0% PVA solution by a high-shear dispersing emulsifier at a speed of 2000 rpm for 2–3 min to form a W/O/W emulsion, and 400 mL of PVA solution (1.0 wt%) was added under stirring. Then, a calculated amount of CuSO4 (1.0 eq. to alkyne group) and NaLAc (1.0 eq. to alkyne group) was added. The MS purification process was the same as that of the drug-free MSs. The supernatant was collected and freeze-dried before re-dissolving it in DI water to measure the free BSA amount.
The BSA release study was conducted by putting 100 mg of BSA loaded MSs in a dialysis tube with a molecular weight cut-off of 20 kDa. The dialysis tube was immersed in 20 mL of PBS (pH 7.4) at 37 °C with shaking. At pre-set time points, 1 mL of PBS solution was taken out, and 1 mL of fresh PBS solution was added. The concentration of BSA in the PBS solution was determined by UV-vis, according to the standard curve obtained at the same time (Fig. 4A).
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