Hongjun
Yang
a,
Junpeng
Zhao
a,
Manqing
Yan
a,
Stergios
Pispas
b and
Guangzhao
Zhang
*ac
aHefei National Laboratory for Physical Sciences at Microscale, Department of Chemical Physics, University of Science and Technology of China, Hefei, P. R. China 230026. E-mail: gzzhang@ustc.edu.cn; Fax: +86-551-3606743; Tel: +86-551-3606763
bTheoretical and Physical Chemistry Institute, National Hellenic Research Foundation, 48 Vassileos Constantinou Ave., 11635, Athens, Greece
cFaculty of Materials Science and Engineering, South China University of Technology, Guangzhou, P. R. China 510640
First published on 19th October 2011
We have synthesized nylon 3 via ring opening polymerization of 2-azetidinone (β-lactam) with 1-tert-butyl-4,4,4-tris(dimethylamino)-2,2-bis[tris(dimethylamino)- phosphoranylidenamino]-2Λ5,4Λ5-catenadi(phosphazene) (t-BuP4) as the catalyst in a mixture of dimethylacetamide (DMAc) and LiCl. The polymers have been characterized by nuclear magnetic resonance spectroscopy (NMR), Fourier transform infrared spectroscopy (FTIR), X-ray diffraction (XRD), laser light scattering (LLS) and viscometry. The synthesized nylon 3 is a linear and crystalline polymer with a molecular weight as high as 105 g mol−1. The intrinsic viscosity ([η]) relates to the weight average molecular weight (Mw) as [η] = 1.02 × 10−4Mw0.91. The effects of solvent, temperature and catalyst concentration on the polymerization have been examined. The molecular weight and yield increases with the amount of LiCl in the polymerization mixture, but both of them decrease with temperature at a temperature above 50 °C. As the catalyst concentration increases, the yield and the molecular weight of nylon 3 decrease. The possible mechanism for the initiation of polymerization is discussed.
Nylon 3 was first synthesized by hydrogen transfer polymerization of acrylamide.12–15 Such nylon 3 is branched, and the presence of an olefinic double bond at its chain end usually decreases its thermal stability.16 The large amount of metal-based initiator used in this procedure is hard to remove after polymerization, which can drastically decreases their thermal stability and other physical properties. In addition, since most of the initiators do not dissolve in a common solvent, the polymerization is heterogeneous and difficult to control.
A series of mono-, bi-, tri- and tetra-substituted poly(β-lactams) have been successfully synthesized by ring opening polymerization with metal catalysts.17–21 However, nylon 3 can not be synthesized viapolymerization of unsubstituted β-lactam with such a metal catalyst. Recently, nylon 3 was synthesized by ring opening polymerization of unsubstituted β-lactam catalyzed by enzyme.22 Unfortunately, its molecular weight was very low. In this work, we have synthesized high molecular weight unsubstituted nylon 3 by the use of a metal-free catalyst, that is, (1-tert-butyl-4,4,4-tris(dimethylamino)-2,2-bis[tris(dimethylamino)-phosphoranylidenamino]-2Λ5,4Λ5-catenadi(phosphazene) (t-BuP4), which was revealed to be a very strong base.23,24 Recently, it was reported that t-BuP4 demonstrates efficiency in catalyzing ring opening polymerizations of oxyalkylenes,25–27ε-lactams,28 cyclopropane-1,1-dicarboxylates,29β-lactones30 and cyclic esters.31t-BuP4 was also used as a complexing agent for butyl lithium to synthesize block polymer.32 Particularly, it is soluble in some common solvents and can work in mild conditions.
Sample | r a | T b (°C) | t c (min) | Yield (%) | M w × 10−4 (g mol−1) d | 〈Rg〉 (nm) | 〈Rh〉 (nm) | 〈Rg〉/〈Rh〉 |
---|---|---|---|---|---|---|---|---|
a Molar ratio of t-BuP4 toβ-lactam. b Reaction temperature. c Reaction time. d Determined by SLS. | ||||||||
Ny1 | 1/200 | 25 | 180 | 96 | 1.12 | 8 | 4 | 2.0 |
Ny2 | 1/333 | 25 | 180 | 86 | 1.22 | 9 | 4 | 2.0 |
Ny3 | 1/500 | 25 | 180 | 80 | 1.27 | 10 | 5 | 2.0 |
Ny4 | 1/2000 | 25 | 180 | 74 | 10.5 | 38 | 17 | 2.2 |
Ny5 | 1/2000 | 50 | 180 | 90 | 12.8 | 40 | 18 | 2.2 |
Ny6 | 1/2000 | 80 | 180 | 54 | 7.66 | 29 | 13 | 2.2 |
Fig. 1 1H NMR spectra of β-lactam and nylon 3 (sample Ny4) in CDCl3/TFA-d3 (5/1, v/v). |
Fig. 2 shows the 13C NMR spectrum of nylon 3 (sample Ny4). Besides the signals about the solvent, we can observe three peaks corresponding to the carbons of linear nylon 3. No any peaks due to branching appear. The facts further indicate that the nylon 3 is linear.
Fig. 2 13C NMR spectrum of nylon 3 (sample Ny4) in CDCl3. |
Effects of solvent, temperature and catalyst concentration on the polymerization have been further examined. DMAc containing 5–10 wt % of LiCl is the best solvent for synthesis of nylon 3. The addition of LiCl to DMAc can improve the polymer solubility so that the molecular weight and yield increases with the amount of LiCl above its solubility. In DMAc without LiCl or in dimethyl sulfoxide (DMSO), precipitation occurs in the initiation stage, and only low molecular weight polymers can be obtained at a limited yield. We also examined the melt polymerization of β-lactam in bulk at 110 °C. Likewise, either the yield or molecular weight of the polymer obtained was low.
We have studied the temperature effect in the range of 25 to 80 °C. At a temperature below 50 °C, white gel is formed during the polymerization, leading to a heterogeneous polymerization system. At a temperature above 50 °C, the system is homogeneous during polymerization. On the other hand, as shown in Table 1, either the molecular weight or yield dramatically decreases with temperature. It is known that t-BuP4 forms a bulky cation during the polymerization, which can suppress the formation of cyclic oligomers.34 However, the bulky cation is probably not stable at a higher temperature so that the reaction equilibrium shifts to cyclic oligomers, leading the molecular weight and yield to decrease.
Catalyst concentration has a considerable effect on the polymerization. Table 1 also shows the dependence of the molecular weight and yield on the molar ratio (r) of t-BuP4 toβ-lactam. As r increases, the concentration of active species increases, so that the polymerization rate increases. However, the molecular weight decreases. This is understandable because the polymerized monomers per active species decrease with the number of active species. A high molecular weight (>105) is achieved at the catalyst/monomer ratio of 1/2000 (mol/mol).
Fig. 3 shows the time dependence of monomer conversion and ln([M]0/[M]), where [M]0 and [M] are the initial monomer concentration and the concentration at a certain time. The polymerization was carried out in DMAc containing 10 wt% of LiCl at 25 °C. The concentration of β-lactam is 1.4 mol L−1, and the molar ratio (r) of catalyst to monomer is 1/2000. The system turns to light yellow as soon as t-BuP4 is added, an indication of formation of lactamate anion or acyllactam anion, implying that the polymerization follows an anionic polymerization mechanism. As expected, the conversion increases with reaction time after t-BuP4 is added. Half of the monomer molecules are converted into polymer chains within 10 min, indicating the high activity of the catalyst. The linear time dependence of ln([M]0/[M]) in the first 10 min demonstrates that the polymerization is of first-order. Namely, the concentration of active species is fairly constant. Conversions close to 50% are achieved at the end of this period.
Fig. 3 Time dependence of conversion and ln([M]0/[M]) at 25 °C. |
It should be noted that the polymerization of β-lactam catalyzed by t-BuP4 does not have an induction period, unlike those with metal catalyst. We characterized the product by FTIR ten seconds after t-BuP4 was added, where the polymerization was terminated by addition of excess of menthol. The occurrence of a band at 1540 cm−1 assigned to amide II in FITR spectra (not shown) indicates that the amide group has already changed from cis to trans configuration due to ring opening in a such short time.18 The rapid conversion demonstrates that t-BuP4 is an efficient promoter for the β-lactam polymerization. Actually, the polymerization catalyzed by t-BuP4 even does not need any other activator. This is quite different from the ring-opening polymerization of β-lactam with metal catalyst, where N-benzoyl derivative, which is much more electrophilic than a β-lactam, is usually used as an activator.
Based on the mechanism proposed before,35 we suggest that the initiation of ring opening polymerization of β-lactam catalyzed by t-BuP4 involves nucleophilic attack of a lactamate anion on the carbonyl group of an imide at the polymer chain end (Scheme 1). Specifically, the initiation involves the following steps. (1) At the beginning, lactam reacts with t-BuP4 (B) to yield a lactamate anion. (2) The lactamate anion reacts with monomer to form an aminic anion with ring opening. (3) The unstable aminic anion quickly abstracts a proton from β-lactam to yield dimeric lactam and regenerate lactamate anion, which acts as the growth center of polymerization. Note that unlike the case of anionic ring opening polymerization with metal catalysts, the lactamate anion transforms into an aminic anion immediately, so that no apparent induction period is observed.
Scheme 1 Initiation process of the polymerization. |
Fig. 4 shows a typical XRD pattern of nylon 3 prepared in this study (sample Ny4). Two peaks concerning the crystalline region can be observed, that is, α form at 2θ = 19.9° and 2θ = 23.6°, corresponding to the crystalline planes (200) and (002) + (202), respectively. Such forms were also observed in nylon 3 synthesized by hydrogen transfer polymerization.2 The crystallinity measured by XRD here is ∼40%. Note that the crystallinity of nylon has dependence on process or condition.
Fig. 4 XRD pattern of nylon 3 (sample Ny4). |
Fig. 5 shows typical TGA and DSC curves of nylon 3. The thermal degradation starts at about 350 °C and the 50% of weight loss is at about 380 °C. The temperatures are higher than those reported before.33 This is because nylon 3 synthesized in this work has a higher molecular weight. Note that we can observe 8% of weight loss at about 150 °C. This is due to the release of water molecules which bind with the amide groups in nylon 3 viahydrogen bonding. The DSC curve shows that nylon 3 has a glass transition temperature (Tg) around 126 °C. Note that DSC measurement was conducted in the range from 25 °C to 200 °C. Further increasing the temperature leads nylon 3 to degrade, so that we cannot observe a melting peak before its decomposition.
Fig. 6 shows a typical Zimm plot for nylon 3 polymers (sample Ny3 in Table 1). The molecular weight and the average radius of gyration 〈Rg〉 measured are 1.05 × 105g mol−1 and 38 nm, respectively. The positive A2 value (∼7.6 × 10−4 mol mL g−2) indicates that HCOOH is a good solvent for nylon 3. Actually, depending on the synthesis conditions, Mw ranges from 1.12 × 104 to 1.28 × 105 g mol−1, and 〈Rg〉 is in the range 8 to 40 nm (Table 1).
Fig. 6 Zimm plot for nylon 3 polymer (sample Ny4) in formic acid at 25 °C, where polymer concentration ranges from 3.0 × 10−3 to 6.0 × 10−3 g mL−1. |
Fig. 7 shows a typical hydrodynamic radius distribution for sample Ny3. The average hydrodynamic radius 〈Rh〉 is 17 nm. In this work, depending on the synthesis conditions, the average hydrodynamic radius ranges from 4 to 18 nm (Table 1). It is known that for uniform non-draining sphere, hyperbranched cluster, and random coil, 〈Rg〉/〈Rh〉 values are ∼0.774, 1.0–1.2, and 1.5–1.8, respectively.36–39 Here, 〈Rg〉/〈Rh〉 is about 2.0–2.4 for nylon 3 (Table 1), indicating that the polymer has a rigid-like structure.
Fig. 7 Hydrodynamic radius distribution (f(Rh)) of sample Ny4 in formic acid. |
We also measured the viscosity of the nylon 3 samples. Fig. 8 shows the relation between intrinsic viscosity [η] and weight average molecular weight (Mw) measured by SLS. Clearly, Mw is scaled to [η]. Namely, it follows the Mark-Houwink equation, [η] = KMα, where K and α are constants, which depend on the nature of the polymer and solvent, as well as temperature. It is well known that α = 0.5 for a polymer in a theta solvent. In a good solvent, 0.5 < α < 0.8 for a flexible polymer, α > 0.8 for a semiflexible polymer, and 1.8 < α < 2.0 for a rigid polymer.40 From the slope and intercept of the line in Fig. 5, we have α = 0.91 and K = 1.02 × 10−4 mL g−1, respectively. Like other polyamides,41nylon 3 has a relatively higher α value, further indicating that the chains have some rigid character, which is consistent with the conclusion from 〈Rg〉/〈Rh〉 values. The intramolecular and intermolecular hydrogen bonding in nylon 3 should be responsible for the chain rigidity.
Fig. 8 Specific viscosity [η] vs. weight molecular weight (Mw) relation. |
This journal is © The Royal Society of Chemistry 2011 |