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Poly(delta-gluconolactone) and Poly(delta-gluconolactone-[epsilon]-caprolactone) from delta-Gluconolactone and [epsilon]-Caprolactone by Ring-Opening Polymerization.

1. Introduction

Glucose is the most important energy source of living cells and intermediate materials of metabolism, which stored as a polymer, in plants as starch and in animals as glycogen [1]. Beside the function in biology, it is used as medicine, food additives, and chemicals [2]. Because of its huge storage in the celluloses, the glucose and its derivatives had a wide range of applications, such as calcium gluconate and zinc gluconate which are used as sequestrants, acidifiers, curing agents, pickling agents, or leavening agents [3, 4]. Although there are extensive researches and applications on the delta-gluconolactone (d-GL), the research on its further chemical reaction, derivatives, and synthesis polymers is relatively rare, especially on its ring-opening polymerization (ROP) reaction. This consequence is partly due to the presence of hydroxyl (-OH) on d-GL that is detrimental for ROP, as it leads to deactivation of the polymerization via undesirable side reaction, such as crosslinking-induced gelation [5, 6]. The polymerization of d-GL into poly(delta-gluconolactone) (PGL) suggested novel potential applications, like drug delivery system by introducing polar functionalities groups (-OH) as well as the functionalities group of the polymers, which can provide anchor for tissue regeneration through cell attachment, proliferation, control of inflammation, and healing.

PGL might be a good affinity for water while poly([epsilon]-caprolactone) (PCL) is hydrophobic. Considering the similar cyclic structure between d-GL and [epsilon]-caprolactone (CL), copolymerization of d-GL with CL could overcome the drawbacks and induce new functionalities, to yield biobased polymers with possible industrial and medical applications [7, 8]. Such polymerization reactions can be accomplished by lipase biocatalysis, and d-GL can be copolymerized with [epsilon]-caprolactone (CL) and [beta]-butyrolactone through immobilized lipases to form an aliphatic oligomer (best experiment m/z value 1587) in previous reports [7, 8]. The aim of present work is to obtain higher molecular weight polymers through chemical method.

To our knowledge, this is the first research in which PGL and P(GL-CL) with high molecular weight were successfully synthesis from d-GL and CL by chemical method. The aim of this work was to discuss synthesis, characterization, and in vitro degradation of PGL and P(GL-CL).

2. Materials and Methods

2.1. Materials. [epsilon]-Caprolactone (CL, Xiya Reagent, 99.9%) was dried with CaH2 (Aladdin Regent, 98.5%) for 24 hours at ambient temperature and by reduced pressure distillation prior to use [9-13]. delta-Gluconolactone (d-GL, Aladdin Reagent, 98%) was dried in vacuum at 80[degrees]C before use. The other reagents, Sn[(Oct).sub.2], tetrabutyl titanate (TBT), dimethyl sulfoxide-[d.sub.6] (DMSO-[d.sub.6]), monobutyltin oxide (MBTO), n-octane, methylbenzene, and diethylene glycol, purchasing from Aladdin Reagent Co., Ltd., were used without further purification. Other reagents from Shanghai Tengzhun Biotechnology Co., Ltd., were used according to the label instructions.

2.2. Synthesis PGL and PCL. In a typical experiment [11, 14], a Schlenk tube equipped with a magnetic stirrer was sequentially charged with catalyst (MBTO, 2 equiv), monomers (CL or d-GL, 1000 equiv), and initiator (diethylene glycol, 1 equiv) in n-octane followed by pumping vacuum and high pure dry nitrogen in turn for three times. Subsequently, the temperature was gradually raised to 160[degrees] C and then reaction was conducted at this temperature for assigned time to obtain PGL. PCL was synthesized through the same procedure except that the polymerization temperature was 140[degrees]C. After the reaction, the n-octane was removed in vacuum and then the target product was purified by dissolving in dichloromethane followed by precipitating in ethanol.

In order to optimize the reaction condition, a series of polymerization reactions of PGL were performed at varying reaction time (4, 6, 8, and 12 h) and temperature (120, 130, 140, 150, 160, and 170[degrees]C) by some general catalysts by various initiator (diethylene glycol) and catalyst (MBTO, Sn[(Oct).sub.2], TBT, Y[[N[(Si[Me.sub.3]).sub.2]].sub.3], Al complexes).

2.3. Synthesis of P(GL-CL) Copolymers. All these P(GL-CL) copolymers with various d-GL/CL ratios (d-GL/CL = 5:5, 4:6, 3:7, 2:8, 1:9) were obtained by one-pot-two-step process (Scheme 1). In short, a Schlenk tube equipped with a magnetic stirrer was charged sequentially with catalyst (MBTO, 2 equiv), initiator (diethylene glycol, 1 equiv), and CL in n-octane followed pumping vacuum and high pure dry nitrogen in turn for three times [15, 16]. Subsequently, the temperature was gradually raised to 140[degrees]C and kept for 4 hours and then d-GL was added to the flask and kept for another 4 hours. After that, the reaction temperature increased to 160[degrees]C and was kept for another 4 hours. After completion of this polymerization, the n-octane was removed in vacuum. The target product was purified and obtained by dissolving in dichloromethane, precipitating in ethanol and drying in vacuum to constant weight, sequentially.

2.4. In Vitro Degradation in PBS. An in vitro degradation study of P(GL-CL) was carried out in phosphate buffered saline (PBS). All the samples were shattered into particles (1100-2000 [micro]m) and soaked in PBS with a weight-to-volume ratio of 1/30 (g [mL.sup.-1]) at 37[degrees] C in a shaking water bath [17]. The incubation time was up to 10 weeks with PBS refreshment every week. The initial weight ([W.sub.0]) of the particles was obtained after the samples were dried in vacuum. The weight ([W.sub.1]) at certain time point was obtained by weighting the specimens after cleaning with water and drying in vacuum. The weight loss ratio of the samples was calculated using the following:

Weight loss ratio = 100% x ([W.sub.0] - {W.sub.1])/[W.sub.0]. (1)

2.5. Characterizations

2.5.1. Fourier Transformed Infrared (FT-IR) of PGL and P(GL-CL). Fourier transformed infrared (FT-IR) spectra were recorded on a Thermo Nicolet IR-100 spectrometer via sample films coated on KBr crystal.

2.5.2. NMR Measurements of PGL. The [sup.1]H NMR spectra were recorded on a Bruker DRX-600 MHz NMR spectrometer using DMSO-[d.sub.6] or [D.sub.2]O as solvent with tetramethylsilane (TMS) as the internal chemical reference. Monomer conversions were calculated from [sup.1]H NMR spectra of the polymer samples from integration (Int.) ratio Int.P(d-GL)/[Int.P(d-GL) + Int.(d-GL)] using the methyne group in the position of the carbonyl (CH, [delta] = 4.11 ppm) for PGL.

2.5.3. Intrinsic Viscosity and Gel Permeation Chromatography (GPC) of Polymers. The intrinsic viscosity measurement of each polymers was carried out in Dimethyl Sulphoxide (DMSO) at 30[degrees] C by Cannon-Ubbelohde viscometer. The intrinsic viscosity values were obtained by a one-point method (the Solomon-Ciuta equation) as follows:

[[eta].sub.int] = [square root of 2 ([[eta].sub.sp] - ln [[eta].sub.r]))]/c, (2)

where [[eta].sub.r] = [eta]/[[eta].sub.0], [[eta].sub.r] = [eta]/[[eta].sub.0] - 1, and c was polymer concentration in DMSO. And the number average ([M.sub.n]) and polydispersity index (PDI) were measured using Water-2414 equipped with a Waters Styragel HT4 and using Dextran as standards with molecular weights from 1.0 x [10.sup.3] to 2.7 x [10.sup.5] g [mol.sup.-1]. THF was used as mobile phase at a rate of 1 mL [min.sup.-1] and the column temperature was 30[degrees]C.

2.5.4. XRD of PGL and P(GL-CL). XRD (Philips X'pert Pro MPD) was used to study the crystalline characteristics of the polymers.

2.5.5. Differential Scanning Calorimetry Analysis (DSC) and Thermogravimetric Analysis (TGA). Differential scanning calorimetry analysis (DSC) was performed on a Perking-Elmer DSC-7 apparatus under nitrogen in the temperature ranging from 0 to 200[degrees]C at a heating rate of 10[degrees]C [min.sup.-1]. The samples were first heated to 160[degrees]C and then cooled to 30[degrees]C by liquid nitrogen, followed by heating to 200[degrees]C at a heating rate of 10[degrees]C [min.sup.-1]. The glass transition temperature ([T.sub.g]) and melting point was recorded from the cooling flow and the second heating run, respectively. The thermogravimetric analysis (TGA) was conducted on PerkinElmer Pyris Diamond thermogravimetric/differential thermal analyser (TG/DTA) at 10[degrees]C [min.sup.-1] from 30 to 600[degrees]C.

3. Results

3.1. ROP of d-GL in Various Conditions. In this study, different reaction catalysts were investigated for ROP of dGL, and the results are shown in Table 1. It was found that some general catalysts for polyester polymerization, like TBT, Sn[(Oct).sub.2], some Al complexes (aluminium isopropoxide, aluminumtriethyl, triisobutylaluminium) and the Rare Earth catalyst Y[[N[(Si[Me.sub.3]).sub.2]].sub.3] prepared as previous reported [18], failed for ROP of d-GL. When monobutyltin oxide (MBTO) was employed as catalyst and reflexed in n-octane at 150[degrees]C for 8 hours under nitrogen, an off-white polymer (PGL) was precipitated from the solution. The obtained polymer was freely soluble in water and some polar solvents (e.g., THF, DMSO, and CH[Cl.sub.3]) but insoluble in alcohol, acetone, and methylbenzene. In addition, various reaction temperature (120, 130, 140, 150, 160, and 170[degrees]C) and reaction time (4, 6, 8, and 12 h) were also investigated in the MBTO catalytic system, summarized in Table 2. It was found that when the temperature was lower than 120[degrees]C, the reaction rate was lower, or the reaction could not proceed. And conversion increasing with rising the polymerization time when temperature was lower than 160[degrees] C. But coloration or decomposition of an aliphatic polyester could be manufactured, when the temperature was higher than 170[degrees]C.

3.2. FT-IR of PGL and P(GL-CL). As shown in Figure 2, the stretching vibration of hydroxyl associated with hydrogen bond shifted from (3468, 3392, 3277, and 3218 [cm.sup.-1]) of d-GL to an enlarged peak (3392 [cm.sup.-1]) in PGL. In addition, compared to d-GL, the deformation peaks of hydroxyl shifted from 1719 to 1736 [cm.sup.-1] in PGL. Moreover, the sharp peaks corresponding to the C=O symmetric stretching vibration of ester linkage shifted from 1719 to 1736 [cm.sup.-1] in PGL, compared with d-GL.

Figure 2 showed the FT-IR spectra of copolymers with various d-GL/CL ratios. It was found that the FT-IR spectra of P(GL-CL) compared to PCL showed a broad-enlarged peak assigned to hydroxyl symmetric stretching vibration around 3526 [cm.sup.-1]. The enlarger hydroxyl peak of P(GL-CL) showed blue-shifted with d-GL/CL ratio increasing, as well as the peaks assigned to C=O symmetric stretching vibration from (1700 to 1750 [cm.sup.-1]).

3.3. NMR Spectra ofPGL. To further investigate the structure of PGL, the [sup.1]H NMR was determined in DMSO-[d.sub.6] and [D.sub.2]O (Figure 3). The [sup.1]H NMR spectrum of PGL was reported as follows: [sup.1]H NMR (600 MHz, DMSO-[d.sub.6], [delta]) 4.11 (d, J = 3.80 Hz, 1H), 4.0 (ddd, J = 2.35, 2.07, 2.18 Hz, 4H), 3.9 (dq, J = 3.51, 2.90 Hz, 1H), 3.65 (dd, J = 2.29, 2.32 Hz, [sup.1]H), 3.58~3.49 (m, 1H), 3.48 (m, 1H), and 3.35 (dd, J = 5.56, 5.38 Hz, 1H). And the peak at [delta] = 4.0 in PGL/DMSO-[d.sub.6] disappeared in [D.sub.2]O. In Figure 2(b), [sup.1]H NMR results of PGL/[D.sub.2]O were listed as follows: [sup.1]H NMR (600 MHz, [D.sub.2]O, [delta]) 4.41 (d, J = 3.16 Hz, 1H), 4.26 (d, J = 4.07 Hz, 4H), 4.08-4.03 (m, 1H), 3.94 (dq, J = 3.51, 3.31 Hz, 4H), 3.75 (dd, J = 2.25, 2.21 Hz, 1H), 3.64 (dd, J = 2.34, 2.78 Hz, 4H), 3.61 (dd, J = 3.47, 2.83 Hz, 2H), 3.58 (dd, J = 2.5, 2.74 Hz, 8H), 3.55 (dd, J = 2.88, 4.99 Hz, 1H), and 3.47 (dd, J = 6.15, 5.51 Hz, 4H).

3.4. The Intrinsic Viscosity and GPC of Homo- and Copolymers. The intrinsic viscosities ([[eta].sub.int]) of polymers (Table 3) (d-GL/CL = 10:0, 5:5, 4:6, 3:7, 2:8, 1:9, and 0:10) were 0.40, 0.46, 0.48, 0.56, 0.70, 0.87, and 1.07, indicating that intrinsic viscosity decreased as d-GL proportion increasing. The molecular weight distributions ([M.sub.n]) measured by GPC were consistent with the intrinsic viscosities and ranged from 1.58 to 2.86 kDa. The molecular distribution of polymer was observed to be monomodal (Figure 4), and the molecular weight ([M.sub.n]) and PDI were summarized in Table 3.

3.5. XRD Curves of PGL and P(GL-CL). Figure 4(a) showed the XRD patterns of the novel polymer PGL was laigh and diffuse, compared to its monomer d-GL. In Figure 4(b), obvious crystallinity peak of PCL appeared around 21.5 and 24[degrees], and the intensity of P(GL-CL) decreased markedly as d-GL/CL ratio increasing. The degrees of crystallinity of P(GL-CL) copolymers (d-GL/CL = 5 : 5, 4 : 6, 3: 7, 2 : 8, 1: 9, and 0: 10) were 12.09, 28.01, 33.42, 38.79, 40.51, and 59.78% (Table 3) obtained by X'pert HighScore software, respectively.

3.6. The Thermal Properties of PGL and P(GL-CL). In Figure 5(a), DSC data of PGL showed that no melting point could be observed during heating flow run and the glass transition peak appeared at 21.4[degrees]C in the cooling flow. In Figure 5(b), compared to melting point peaks of PCL appearing around 62.0[degrees]C, the DSC curves of P(GL-CL) copolymers started to split off into double peaks at slightly lower than melting point of PCL homopolymer, and it became more obvious as d-GL/CL ratio increases. In particular, the DSC curve of the copolymer (d-GL/CL = 5:5) showed split-off peak at 49.8 and 55.8[degrees]C and it showed continuous decline at higher temperature. And the first melting point of copolymers (d-GL/CL = 1: 9, 2: 8, 3 : 7, 4: 6, and 5 : 5) were 54.0, 53.2, 53.1, 52.7, and 49.8[degrees]C, respectively.

In Figure 5(c), the TGA curses showed initiate and decomposition degradation temperatures of PGL were 222 and 299[degrees]C, respectively, while PCL's initiate and decomposition temperatures were 282 and 347[degrees]C. It can also be seen that a flight of double stages existed in the TGA curves of P(GL-CL) copolymers and it became more blurred as d-GL/CL ratio increasing; notably, the copolymers with d-GL/CL molar ratio of 5: 5 showed continuous slowly decline. The degradation temperature of P(GL-CL) was widened, for which decomposition degrade temperatures of copolymers (d-GL/CL = 5:5, 4:6, 3:7, 2:8, 1:9) were 459, 453, 432, 425, and 415[degrees]C, much higher than PCL and PGL, respectively.

3.7. In Vitro Degradation. The weight loss of PGL and P(GL-CL) immersed in PBS solution over time was shown in Figure 6(a). It could be found that all the samples, except PCL, had a quick weight loss in the initial 2 weeks, followed by a slightly slow weight loss and PGL was easily dissolved in PBS. The weight loss of polymers (d-GL/CL = 0 : 10, 1: 9, 2: 8, 3: 7, 4: 6, and 5: 5) were 0.4, 9.1, 19.7, 23.7, 33.6, and 56.2 wt% in the first week and 6.8, 24.9, 35.7, 45.9, 52.3, and 73.5 wt% at the end of the experiment, respectively. With d-GL content increasing in the main chain, the degradation of P(GL-CL) was significantly accelerated. And the degradation rate of copolymers gradually decreased as soaking time increasing; finally the rate of weight loss of copolymers was consistent with the PCL. Figure 6(b) expressed the pH changes of polymers (d-GL/CL = 0 : 10, 1: 9, 2: 8, 3 : 7, 4 : 6, 5 : 5) were 7.2, 5.9, 3.8, 2.4, and 2.1 at the first week, respectively, during soaking and the pH of PGL dissolved in PBS was 1.6. And the neutral pH of copolymers was achieved gradually at the end of the experiment.

4. Discussion

In this work, the d-GL was successfully catalyzed by MBTO into polymer without hydroxyl protection and deprotection and copolymerization with CL through one-pot-two-step process. But it was failed to polymerize d-GL into PGL through melt polymerization and by some general catalysts which could easily catalyst CL into PCL [14, 19, 20]. Noticed common polarity solvents, such as THF, DMSO, and CH[Cl.sub.3], caused crosslinking and gelation in the ROP process of d-GL into PGL (Table 1). The reason why P(GL-CL) copolymer could not synthesis through one-pot-one-steps process might be that the coloration or decomposition of polymer was induced by the polar dissolvability of CL. However, in the one-pot-two-step process, most of CL was catalyzed into PCL before d-GL was added to the reaction system, so it could be avoiding some side reaction of d-GL induced by the polar dissolvability of CL. Considering the effect of temperature (Table 2), the polymerization temperature of PGL was up to 130 to 170[degrees]C, because the melting point of d-GL was 151 to 155[degrees]C. When the temperature was lower than 120[degrees]C, the reaction rate was lower, or the reaction could not proceed. And coloration or decomposition of an aliphatic polyester could be manufactured [21], when the temperature was higher than 170[degrees]C. Thus, the favorable reaction temperature of PGL might be 150 to 160[degrees]C, and the reaction system should be limited to reflex in n-octane due to the boiling point of n-octane was 125[degrees]C. The favorable polymerization time might be 4-6 h in consideration of catalyst d-GL into PGL.

In Figure 1(a), it is obvious to observe that all bands ascribed to hydroxyl, for stretching vibration at 3392 [cm.sup.-1] and for deformation vibration at 1226 [cm.sup.-1], shifted to enlarged peaks in PGL, compared with d-GL, indicating that associated hydroxyl existed in PGL's structure after ROP. And the C=O vibration peak of PGL was band reshifted from 1719 to 1736 [cm.sup.-1], indicating C=O group was substituted with electron donating in ROP process (Scheme 2). From Figure 1(a), peak at [delta] = 4.0 (ddd, J = 2.35, 2.07, 2.18 Hz, 4H) was observed as a steamed bun and tripeak, indicating the hydroxyl attached to three kinds of carbons (CH, CHH, CHH), and it disappeared in [D.sub.2]O due to hydroxyl exchange with solvent formed HDO [22], and it is easily observed PGL slow degradation into glucose acid in Figure 2(b). All these results are of FT-IR and [sup.1]H NMR; it is most likely the desired product obtained was successful, and hydroxyl was protected in the whole syntheses process [6]. Along with d-GL/CL ratio increasing in P(GL-CL), the absorption peaks assigned hydroxyl of P(GL-CL) became more obvious and shifted to lower wavenumbers, indicating that hydroxyl was protected and undesirable reaction did not occur in the whole reaction. The same blue-shift phenomenon was observed at the peaks assigned C=O symmetric stretching vibration of P(GL-CL) and the GPC curves of all these P(GL-CL) were observed to be monomodal, demonstrating that the resulting products are a copolymer in nature not a mixture of PCL and PGL [23], so d-GL was copolymerized with CL successfully.

The mechanistic of ROP (Scheme 2) was hypothesized according to previously disclosed publication [18, 24-26], which follows typical coordination-insertion mechanism. At first, MBTO formed active species with initiator; then the active species ring-opening d-GL in the chain propagation step and dormant chain were formed by isolating MBTO segment in the chain growing process. As discussed in abovementioned, it was the carbonyl oxygen rather than ether oxygen of d-GL that firstly coordinates with active species during the coordination polymerization, because C=O group substituted with electron donating in FT-IR spectrum of PGL (Figure 1(a)) [26]. And the possibility of primary hydroxyl of d-GL participating in the reaction process could not be excluded because the [sup.1]H NMR (Figure 2(a)) showed much clutter from 3.48 to 3.43 ppm. This hypothesis can be further confirmed by the experiment (Table 1, Entry (10)), which PGL also could be obtain in the reaction system without initiator. In that case, the primary hydroxyl of d-GL might be replacing hydroxyl of initiator in the reaction system. But in [D.sub.2]O, PGL could be slowly degrading to glucose acid, indicating that some undesirable reaction did not occur in ROP of d-GL.

The copolymerization of d-GL with CL underwent a similar manner of ROP (Scheme 3). When CL monomer was consumed to some extent and PCL segment was long enough, d-GL could competitively replace CL to insert into the polymer chain, leading to block copolymer poly(GL-CL). In the PCL or PGL dominant component, the other less content unit as a defect existed in chain structure. This hypothesis block chain could be proved by TGA of P(GL-CL), which showed two kinds of stages.

From results of GPC (Figure 3, Table 3), the PDI of polymers was ranged from 1.16 to 1.41, indicating a narrow molecular weight distribution of the PGL. Compared to PCL, [M.sub.n] of polymers was shown to be decreasing as the ratio of d-GL/CL increasing, which might be related to the fact that reactivity of d-GL's six-membered ring structure was relatively lower than CL's seven-membered structure [26]. All P(GL-CL)'s GPC curves were observed to be monomodal, demonstrating the resulting products were a copolymer instead of mixtures of PCL and PGL [23].

The DSC data (Figure 5(a)) of PGL showed that no melting point ([T.sub.m]) was found in heating flow and XRD curves (Figure 4) of PGL was laigh and diffuse, indicating PGL belongs to amorphous structure. Likewise, the XRD curves (Figure 4) of P(GL-CL) became more laigh and diffuse as d-GL content increasing, showing lower crystallinity of P(GL-CL). And DSC curves of P(GL-CL) split-off more obvious as d-GL/CL ratio increasing at the slightly lower than pure PCL (62.0[degrees]C) and showed continuous decline at higher temperature. These results could be caused by semicrystalline PCL that cannot form a eutectic with amorphous PGL and both homopolymer chain segments were long enough in block chain structure, which are two representatives of melting generated by each segment.

In Figure 5(c), below 222[degrees]C, the PGL loses ca.7% of its weight, suggested PGL crosslinking at high temperatures and low humilities was accompanied by a loss of water. And the backbone thermal degradation temperature of PGL was between 222 and 299[degrees]C. However, the decomposition temperature of P(GL-CL)s was higher than both PCL and PGL. The reason might be that endothermic of PGL segment thermal degradation at first and the PCL segment was protected from backbone thermal degradation. This phenomenon could be explained by the block copolymer structure, which segment with longer PGL start thermal degradation at first and thermal degradation endothermic process protected the shorter one, even leading a slowly continuous decline in TGA curves of P(GL-CL) (d-GL/CL = 5: 5). The TGA results showed that both PGL and P(GL-CL) had good thermal stability.

Because of pendant hydroxyl of d-GL, P(GL-CL) with more PGL segment could be continually hydrolyzed, resulting in quick hydrolysis and degradation. And the PGL segment in P(GL-CL) also reduced the molecular chain regularity, and this reinforces the short range hydration during the incubation in the PBS and enhanced the hydrophilic. As a result, the higher content of PGL segment in P(GL-CL) copolymers showed more degradation than that of PCL. The degradation of P(GL-CL) in the present research showed 6.8 to 73.5 wt% in the 10-week soaking in PBS with deferent d-GL/CL molar ratios. So degradation rates of polyesters could be further adjusted based on the d-GL/CL proportion. This would great improve the degradation of the PCL and extend its application.

5. Conclusions

PGL and P(GL-CL) have been successfully synthesized without hydroxyl protection and deprotection. The obtained PGL was amorphous, had a good thermal stability and hydrophily, and could degrade into glucose acid. Because the polar hydroxyl was introduced into P(GL-CL) copolymers, the hydrolytic degradation rate is significantly changed. Moreover, the eutectic cannot have form in P(GL-CL), resulting in the fact that the thermal properties have a tremendous change. Therefore, PGL and P(GL-CL) may be novel absorbable biomaterials because they have tunable biodegradability, as well as good physical and chemical properties, being worthy of being further evaluated in vivo and in vitro.

https://doi.org/10.1155/2018/5381582

Conflicts of Interest

The authors declare that there are no conflicts of interest related to this paper.

Acknowledgments

This work was supported by the National High Technology Research and Development Program 863 (Grant no. 2015AA033605).

References

[1] D. L. Cutler, C. G. Gray, S. W. Park, M. G. Hickman, J. M. Bell, and O. G. Kolterman, "Low-carbohydrate diet alters intracellular glucose metabolism but not overall glucose disposal in exercise-trained subjects," Metabolism, vol. 44, no. 10, pp. 1264-1270, 1995.

[2] P. B. Ernst, J. C. Garrison, and L. F. Thompson, "Much ado about adenosine: Adenosine synthesis and function in regulatory T cell biology," The Journal of Immunology, vol. 185, no. 4, pp. 1993-1998, 2010.

[3] S. Saka and T. Ueno, "Chemical conversion of various celluloses to glucose and its derivatives in supercritical water," Cellulose, vol. 6, no. 3, pp. 177-191, 1999.

[4] Maria M. J. A., "Animal feed composition containing encapsulated glucono delta-lactone: WO," Animal feed composition containing encapsulated glucono delta-lactone: WO, WO/2013/133713[P], 2013.

[5] B. J. Kline, E. J. Beckman, and A. J. Russell, "One-step biocatalytic synthesis of linear polyesters with pendant hydroxyl groups," Journal of the American Chemical Society, vol. 120, no. 37, pp. 9475-9480, 1998.

[6] P. Zinck, "One-step synthesis of polyesters specialties for biomedical applications," Reviews in Environmental Science and Bio/Technology, vol. 8, no. 3, pp. 231-234, 2009.

[7] A. Todea, E. Biro, V. Badea et al., "Optimization of enzymatic ring-opening copolymerizations involving S-gluconolactone as monomer by experimental design," Pure and Applied Chemistry, vol. 86, no. 11, pp. 1781-1792, 2014.

[8] A. Todea, V. Badea, L. Nagy, S. Keki, C. G. Boeriu, and F. Peter, "Biocatalytic synthesis of [delta]-gluconolactone and [epsilon]-caprolactone copolymers," Acta Biochimica Polonica, vol. 61, no. 2, pp. 205-210, 2014.

[9] A. Todea, V. Badea, L. Nagy, S. Keki, C. G. Boeriu, and F. Peter, "Regular paper Biocatalytic synthesis of S-gluconolactone and [epsilon]-caprolactone copolymers," Acta Biochimica Polonica, vol. 61, no. 2, pp. 205-210, 2014.

[10] Y. Ren, Z. Wei, X. Leng, Y. Wang, and Y. Li, "Boric acid as biocatalyst for living ring-opening polymerization of [epsilon]- caprolactone," Polymer (United Kingdom), vol. 78, pp. 51-58, 2015.

[11] A. Harada, M. Osaki, Y. Takashima, and H. Yamaguchi, "Ring-opening polymerization of cyclic esters by cyclodextrins," Accounts of Chemical Research, vol. 41, no. 9, pp. 1143-1152, 2008.

[12] W. Choi, J. W. Chung, and S.-Y. Kwak, "Total-molecular-weight-dependent Rouse dynamic of ultra-small branched star poly([epsilon]-caprolactone)s as a single coarse-grain unit," Polymer (United Kingdom), vol. 79, pp. 91-98, 2015.

[13] J. Li, Y. Deng, S. Jie, and B.-G. Li, "Zinc complexes supported by (benzimidazolyl)pyridine alcohol ligands as highly efficient initiators for ring-opening polymerization of [epsilon]-caprolactone," Journal of Organometallic Chemistry, vol. 797, Article ID 19190, pp. 76-82, 2015.

[14] J.-B. Fan, K. Yang, H.-Q. Yiet al., "Tetrabutyltitanate-controlled polymerization of [epsilon]-caprolactone at ambient temperature," Chemical Communications, vol. 46, no. 31, pp. 5805-5807, 2010.

[15] R. Zhang, L. Zhang, J. Wang, and X. Guo, "Ring-opening copolymerization of [epsilon]-caprolactone with 2, 2-dimethyltrimethylene carbonate using N-heterocyclic carbene organocatalysts," Polymer Bulletin, vol. 70, no. 4, pp. 1289-1301, 2013.

[16] J. Fernandez, A. Etxeberria, and J.-R. Sarasua, "In vitro degradation studies and mechanical behavior of poly([epsilon]-caprolactone-co- [delta]-valerolactone) and poly([epsilon]-caprolactone-coL-lactide) with random and semi-alternating chain microstructures," European Polymer Journal, vol. 71, pp. 585-595, 2015.

[17] J. Tams, C. A. P. Joziasse, R. R. M. Bos, F. R. Rozema, D. W. Grijpma, and A. J. Pennings, "High-impact poly(l/d-lactide) for fracture fixation: in vitro degradation and animal pilot study," Biomaterials, vol. 16, no. 18, pp. 1409-1415, 1995.

[18] M. Hong and E. Y.-X. Chen, "Completely recyclable biopolymers with linear and cyclic topologies via ring-opening polymerization of y-butyrolactone," Nature Chemistry, vol. 8, no. 1, pp. 42-49, 2016.

[19] P. Lecomte and C. Jerome, "Recent developments in ring-opening polymerization of lactones," Synthetic Biodegradable Polymers, vol. 15, pp. 173-217, 2011.

[20] J. Wu, T.-L. Yu, C.-T. Chen, and C.-C. Lin, "Recent developments in main group metal complexes catalyzed/initiated polymerization of lactides and related cyclic esters," Coordination Chemistry Reviews, vol. 250, no. 5-6, pp. 602-626, 2006.

[21] M. Minami, Aliphatic polyester, method for manufacturing aliphatic polyester, and method for recycling cellulose: EP, US6420513 [P], 2002.

[22] E. C. W. Clarke and D. N. Glew, "Evaluation of Unbonded O--H Groups for HDO in Liquid [D.sub.2]O from Infrared," Canadian Journal of Chemistry, vol. 50, no. 11, pp. 1655-1665, 2011.

[23] J. S. Cho, B. S. Kim, H. Hyun et al., "Precise preparation of four-arm- poly(ethylene glycol)-block-poly(trimethylene carbonate) star block copolymers via activated monomer mechanism and examination of their solution properties," Polymer Journal, vol. 49, no. 7, pp. 1777-1782, 2008.

[24] Y. Feng and J. Guo, "Biodegradable polydepsipeptides," International Journal of Molecular Sciences, vol. 10, no. 2, pp. 589-615, 2009.

[25] F. E. Kohn, J. G. Van Ommen, and J. Feijen, "The mechanism of the ring-opening polymerization of lactide and glycolide," European Polymer Journal, vol. 19, no. 12, pp. 1081-1088, 1983.

[26] Y. Xu, S. Wang, L. Lin, M. Xiao, and Y. Meng, "Semi-crystalline terpolymers with varying chain sequence structures derived from CO2, cyclohexene oxide and [epsilon]-caprolactone: One-step synthesis catalyzed by tri-zinc complexes," Polymer Chemistry, vol. 6, no. 9, pp. 1533-1540, 2015.

Ruijiang Li, (1) Peng Wang, (1) Haohao Ren, (2) Hong Li, (1) Zhengwen Ding, (2) and Yonggang Yan (1)

(1) College of Physical Science and Technology, Sichuan University, Chengdu 610064, China

(2) Testing & Analysis Center, Sichuan University, Chengdu 610064, China

Correspondence should be addressed to Yonggang Yan; yan_yonggang@vip.163.com

Received 15 October 2017; Accepted 9 December 2017; Published 6 February 2018

Academic Editor: Atsushi Sudo

Caption: Figure 1: FT-IR spectra of polymers and d-GL: (a) ((A) d-GL; (B) PGL); (b) ((A) PCL; (B)~(F) d-GL/CL = 1:9; 2:8; 3:7; 4:6; 5:5; (G) PGL).

Caption: Figure 2: [sup.1]H NMR spectrum of the PGL. This PGL was operated under the condition of MBTO as catalyst and diethylene glycol as initiator in n-octane, 160[degrees]C, 4h ((a) DMSO-[d.sub.6]; (b) [D.sub.2]O).

Caption: Figure 3: GPC traces of polymers synthesized with varying d-GL/CL ratios.

Caption: Figure 4: XRD of polymers and d-GL: (a) ((A) d-GL; (B) PGL); (b) polymers with various d-GL/CL ratio.

Caption: Figure 5: DSC and TGA curves of polymers. (a) DSC of PGL in heat and cooling flow; (b) DSC of polymers ((A) PCL; (B)~(F) d-GL/CL = 1: 9; 2: 8; 3 : 7; 4: 6; 5 : 5; (G) PGL); (c) TGA of polymers ((A) PCL; (B)~(F) d-GL/CL = 1:9; 2:8; 3:7; 4:6; 5:5; (G) PGL).

Caption: Figure 6: Hydrolytic degradation of polymers in PBS solution as function of time. (a) Weight loss of polymers ((A) PCL; (B)~(F) d-GL/CL = 1 : 9; 2: 8; 3 : 7; 4: 6; 5 : 5; (G) PGL)); (b) pH of PBS solution.

Caption: Scheme 1: The one-pot-two-step process of P(GL-CL) copolymer preparation.

Caption: Scheme 2: Proposed mechanism for the ROP of d-GL using diethylene glycol as initiator and MBTO as catalyst.

Caption: Scheme 3: Proposed mechanism for the copolymerization of d-GL and CL.
Table 1: Catalysts, solvents and initiators were used
for ROP of d-GL.

Entry     Solvent                   Catalyst

(1)         THF                       MBTO
(2)        DMSO                       MBTO
(3)    CH[Cl.sub.3]                   MBTO
(4)      n-Octane                     MBTO
(5)      n-Octane               Sn[(Oct).sub.2]
(6)      n-Octane                     TBT
(7)         CL                        MBTO
(8)    Methylbenzene                  MBTO
(9)      n-Octane      Y[[N[(Si[Me.sub.3]).sub.2]].sub.3]
(10)     n-Octane                     MBTO
(11)     n-Octane                 Al complexes
(12)   Methylbenzene                  MBTO

Entry      Initiator        Result

(1)    Diethylene glycol      --- (a)
(2)    Diethylene glycol      ---
(3)    Diethylene glycol      ---
(4)    Diethylene glycol   Off-white
(5)    Diethylene glycol      ---
(6)    Diethylene glycol      ---
(7)    Diethylene glycol      ---
(8)    Diethylene glycol   Off-white
(9)    Diethylene glycol      ---
(10)          ---          Off-white
(11)   Diethylene glycol      ---
(12)    Benzyl alcohol     Off-white

(a) --- reaction cannot carry out or cross-linking and gelation occur.

Table 2: ROP of d-GL with various time and temperature
in MBTO catalytic systema.

        Temperature/
Entry    [degrees]C    Time/h   Conversion (b)/%

(1)         120          24           ---
(2)         130          8            48.2
(3)         130          12           56.8
(4)         140          4            51.3
(5)         140          6             63
(6)         140          8            61.7
(7)         150          4             69
(8)         150          6            78.3
(9)         150          8            84.2
(10)        160          4            91.6
(11)        160          6            89.7
(12)        170          4            78.3

(a) All reactions were performed in n-octane with MBTO,
[d-GL]/[Cat] = 500: 1, monomer : initiator = 1000: 1.
(b) Calculated by integration of methane resonances in
[sup.1]H NMR of PGL (DMSO-[d.sub.6], 600 MHz).

Table 3: The properties of polymers with varying d-GL/CL ratios.

         d-GL/CL
          ratio
         in the          Intrinsic
          feed           viscosity
Entry   (mol) (a)   ([[eta].sub.int] (b))   [X.sub.c.sup.c] (%)

(1)        10:0             0.40                    ---
(2)        5:5              0.46                   12.09
(3)        4:6              0.48                   28.01
(4)        3:7              0.56                   33.42
(5)        2:8              0.70                   38.79
(6)        1:9              0.87                   40.51
(7)        0:10             1.07                   59.78

                           Polydispersity
         [M.sub.n.sup.d]/     index (d)
Entry    g x [mol.sup.-1]       (PDI)

(1)           15814              1.27
(2)           18116              1.16
(3)           21675              1.41
(4)           22752              1.33
(5)           25524              1.40
(6)           28631              1.35
(7)           49901              1.36

(a) This PGL and P(GL-CL) were operated under the condition
of MBTO as catalyst and diethylene glycol as initiator in
n-octane. (b) The viscosity of polymers was carried out in DMSO
at 30[degrees]C by Ubbelohde viscometer. (c) Determined by
XRD spectra. (d) Determined by GPC.
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Title Annotation:Research Article
Author:Li, Ruijiang; Wang, Peng; Ren, Haohao; Li, Hong; Ding, Zhengwen; Yan, Yonggang
Publication:International Journal of Polymer Science
Date:Jan 1, 2018
Words:5820
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