Yixin Rena,
Justin T. Millera,
Stefanie T. Poldermana,
Trinh D. Voa,
Adele C. M. Wallacea,
John Michael O. Cuea,
Sarah T. Trana,
Michael C. Biewera and
Mihaela C. Stefan*ab
aDepartment of Chemistry and Biochemistry, The University of Texas at Dallas, 800 W. Campbell Rd., Richardson, TX 75080-3021, USA. E-mail: mci071000@utdallas.edu
bDepartment of Bioengineering, The University of Texas at Dallas, 800 W. Campbell Rd., Richardson, Texas 75080-3021, USA
First published on 24th January 2019
Neodymium-based Ziegler–Natta type catalytic systems are known to produce polydienes with high cis-1,4 content. It is generally believed that in Ziegler–Natta catalytic systems, a halide or pseudohalide, whether in the catalyst itself or a separate source, is required for the success of the polymerization. In this work, we have synthesized an unusual halide-free neodymium diethyl phosphate catalyst for diene polymerization. This neodymium complex combined with triisobutylaluminum (TIBA), formed a binary catalytic system and was used to polymerize β-myrcene. The catalytic system displays high stereospecificity and produces poly(β-myrcene) with 96% cis-1,4 content and a relatively narrow molecular weight distribution (Mw/Mn = 1.80). Also, kinetic studies indicated the catalytic system gives a pseudo-living polymerization. The block copolymer poly(β-myrcene)-b-poly(isoprene) was successfully synthesized by sequential monomer addition, further demonstrating the pseudo-living nature of polymerization with the neodymium diethyl phosphate catalyst.
Lanthanide-based Ziegler–Natta catalysts have drawn particular interest due to higher cis-1,4 microstructure (98%) generated in the polymerization of 1,3-butadiene as compared to catalysts based on transition metals, such as titanium, cobalt, and nickel.4,6–9 Among the lanthanide series, neodymium-based catalysts have been the focus of research due to their better catalytic activities and higher stereoregularity.4,7,10,11 Ziegler–Natta catalysts, including most neodymium catalysts, are generally shown to require halides for alkylation and activation. In many cases, the halides are present in the catalyst itself, resulting in a binary system (along with the alkylaluminum co-catalyst). These catalysts contain electron donor ligands such as isopropanol,12 tributyl phosphate,13 triethyl phosphate,14,15 and tetrahydrofuran (THF).16 In other cases, the catalysts do not have any halide atoms coordinated to the metal and require an additional halide source, such as AlEt2Cl, forming a ternary catalytic system. These catalysts contain carboxylate ligands such as versatates,17,18 octanoates,19 and naphthenates.20 In recent studies, the halogens have been replaced with pseudohalogens, such as borohydrides, and the systems have retained effective catalytic activities.21,22
The catalytic systems without halides usually produce polydienes with low cis-1,4 content and broad molecular weight distribution.23,24 For example, Evans and co-workers studied the chloride effects in a neodymium carboxylate-based catalyst for isoprene polymerization and demonstrated that the catalytic system with a chloride source exhibited a narrower, monomodal molecular weight distribution (Mw/Mn = 2.9–13.5) as compared to the system without chloride, which had a much broader and bimodal molecular weight distribution (Mw/Mn = 14.3–19.8).23 Masuda et al. reported a halide-free binary system consisting of neodymium isopropoxide and methylaluminoxane which polymerized isoprene with only 92% cis-1,4 content.24
In this study, we report the synthesis of a halide-free neodymium diethyl phosphate complex obtained by azeotropic distillation. This complex, in combination with the co-catalyst triisobutylaluminum (TIBA), constitutes a new type of halide-free Ziegler–Natta catalytic system with high cis-1,4 (96%) selectivity and relatively narrow molecular weight distribution (Mw/Mn = 1.8) for the polymerization of β-myrcene. β-Myrcene (7-methyl-3-methyleneocta-1,6-diene, C10H16), was used for this study because it is an environmentally benign, bio-renewable monomer derived from plants such as dill, thyme, and rosemary.25 The high cis-1,4 selectivity and narrow molecular weight distribution are directly influenced by the amount of co-catalyst present in the catalytic system. These results are in contrast to conventional Ziegler–Natta systems in which the halides are required for good performance. Kinetics experiments are performed to demonstrate the pseudo-living behavior of this catalytic system. The successful synthesis of the block copolymer poly(β-myrcene)-b-poly(isoprene) further demonstrates living behavior.
In contrast, our method can easily synthesize the neodymium catalyst in a preparative quantity and high purity. The neodymium catalyst is stable to air, water, and heat, and it is readily soluble in water. EDX analysis further demonstrated the neodymium-complex is halide-free and showed the content of oxygen: 37.03%, neodymium: 3.87%, carbon: 47.25% and phosphorus: 11.87% (Fig. S2 in ESI†).
The polymerization of β-myrcene was systematically investigated using the synthesized catalyst, [Nd(μ-DEP)3]x, and several controls, including the precursor (NdCl3·6H2O) and both with and without TIBA as a co-catalyst, a control experiment using only TIBA, and the catalyst without TIBA. The experimental results are summarized in Table S1 in ESI.† The results indicated that both NdCl3·6H2O and [Nd(μ-DEP)3]x were not catalytically active when used alone. The combination of NdCl3·6H2O/TIBA likewise produced only a trace amount of polymer. The use of only TIBA resulted in a highly cross-linked insoluble polymer. However, the combination of [Nd(μ-DEP)3]x and TIBA effectively efficiently polymerized β-myrcene. This catalytic system is similar to the Ziegler–Natta catalytic system and is active towards diene polymerization only in the presence of an organo-aluminum compound as a co-catalyst, with the exception that halides are not necessary for the polymerization.
Despite the lack of halides, our catalytic system exhibits relatively narrow molecular weight distribution (Mw/Mn = 1.8), and comparatively high cis-1,4 content up to 96% for the polymerization of β-myrcene. In contrast, other previously reported binary systems with an absence of halides produced large polydispersity indexes, bimodal molecular weight distributions, and much lower cis-1,4 content.23,24
Several organoaluminum cocatalysts were tested, including triisobutylaluminum (TIBA), methyl aluminoxane (MAO), and the combination of TIBA/diethyl aluminum chloride (DEAC). However, TIBA is the most effective toward the polymerization of β-myrcene and results in the highest molecular weight with a relatively narrow PDI and highest content of cis-1,4. The neodymium to TIBA ratios were systematically varied to achieve the optimal conditions for polymerization, and the results are summarized in (Table 1, entry 1–6). The molar ratio of [Nd]:[TIBA] = 1:30 produced the best results for the polymerization of β-myrcene, producing a molecular weight of 13000 and PDI of 1.80 and affording cis-1,4 content of 96% (Table 1, entry 5). The synthesized poly(β-myrcene) was characterized by 1H and 13C NMR analysis (Fig. S3, in ESI†). When polymerizing the diene monomers, typically three different microstructures of the polymers could occur that are cis-1,4, trans-1,4, and 3,4 isomers. The content of cis-1,4 and 3,4 isomers of poly(β-myrcene) was determined using 1H NMR analysis by integrating the peak at 5.1 ppm which is due to protons from the cis-1,4 product, against the peak at 4.9 ppm which is corresponding to the protons from 3,4 incorporation. The presence of trans-1,4 incorporation can be identified in 13C NMR at 131.6 ppm, however, with this catalytic system, no trans-1,4 incorporation of the poly(β-myrcene) was observed.
Entry | [My]0:[[Nd(μ-DEP)3]x]0:[TIBA]0 | Conversion (%) | Mn (g mol−1) | PDI | cis-1,4 (%) | |
---|---|---|---|---|---|---|
1 | 250:1:3 | 26 | 6835 | 2.38 | 95 | |
2 | 250:1:10 | 27 | 3460 | 1.98 | 95 | |
3 | 250:1:20 | 56 | 5950 | 2.45 | 95 | |
4 | 250:1:25 | 74 | 9455 | 2.35 | 96 | |
5 | 250:1:30 | 98 | 13000 | 1.80 | 96 | |
6 | 250:1:35 | 98 | 5265 | 3.10 | 95 |
The molecular weight distribution is relatively narrow for this catalytic system. One possible reason for this could be that the reaction mixture becomes homogeneous upon addition of TIBA (Fig. S4, in ESI†). This could be attributed to more alkyl segments from TIBA coordinated to the metal, which increases the solubility. The mixture remains homogenous after the addition of monomer. Because of this, each active site is identical and immediately available, without concerns of microenvironment effects or the catalyst becoming more accessible over time. Consequently, the molecular weight distribution is narrower than in a heterogeneous system.
To probe the polymerization behavior, the polymerization of β-myrcene with [Nd(μ-DEP)3]x catalyst was performed at room temperature with various molar ratios of monomer to neodymium catalyst to TIBA co-catalyst including 150:1:30, 250:1:30, 500:1:30, and 1000:1:30 to evaluate the dependence of molecular weight on the monomer to initiator ratio (Table 2, entry 1–4). It is observed that the molecular weight of the synthesized poly(β-myrcene) depended on the molar ration of monomer to neodymium and increased with increasing β-myrcene to neodymium ratio. For example, the ratio of 150:1 produced a molecular weight of polymer 6700 g mol−1 (Table 2, entry 1), and increasing the ratio to 1000:1, the molecular weight of polymer increased to 48500 g mol−1 (Table 2, entry 4). The molecular weight versus the monomer to initiator ratio plot is shown in Fig. S5 in ESI.† The observed molecular weight in SEC is lower than the predicted molecular weight could be in part due to the difference between the hydrodynamic volume of poly(β-myrcene) and the polystyrene standard that was used to calibrate the SEC.
Entry | [M]0:[[Nd(μ-DEP)3]x]0:[TIBA]0 | Conversion (%) | Mn (g mol−1) | PDI | cis-1,4 (%) |
---|---|---|---|---|---|
1 | 150:1:30 | 95 | 6700 | 2.25 | 96 |
2 | 250:1:30 | 98 | 13000 | 1.80 | 96 |
3 | 500:1:30 | 98 | 27125 | 3.88 | 96 |
4 | 1000:1:30 | 60 | 48500 | 4.63 | 96 |
Kinetic studies were performed using a molar ratio of [Nd]:[TIBA]:[β-myrcene] = 1:30:250 at 24 °C over two hours. The slight deviation from linearity in Fig. 1a could indicate the presence of some termination reaction, and a slow initiation based on the shape of the logarithm of the monomer conversion plot. Similarly, slow initiation was also observed in a previously reported catalytic system containing NdCl3·3TEP in our group.14 The polydispersity index decreases as the conversion increases, as shown in Fig. 1b. The number average molecular weight as a function of conversion deviated slightly from linearity (Fig. 1b), indicating a small contribution of chain transfer reactions, a departure from ideal living polymerization behavior. Therefore, we consider this catalytic system is pseudo-living. The conversion versus time plot (Fig. S6 in ESI†) indicates the conversion of monomer reached approximately 95% in two hours.
Fig. 1 (a) Logarithm of monomer conversion versus time, (b) Mn and PDI versus conversion. Reaction conditions: room temperature, at the molar ratio of [M]:[[Nd(μ-DEP)3]x]:[Al] = 250:1:30. |
Chain extension experiments further demonstrate the living behavior of the [Nd(μ-DEP)3]x/TIBA catalytic system. The initial portion of monomer was polymerized at a molar ratio of [β-myrcene]:[[Nd(μ-DEP)3]x]:[TIBA] = 150:1:30. Upon the complete consumption of the monomer, the second portion of β-myrcene, twice the amount of the first batch (300 equivalents), was introduced. If the catalytic system exhibited living character, the molecular weight after the complete consumption of the second portion of the monomer is expected to triple. The SEC traces shown in Fig. 2 indicated the monomodal distribution and the molecular weight increase from 6700 g mol−1 to 21650 g mol−1 after the addition of the second portion of β-myrcene. The small tailing observed in the low molecular weight on the SEC traces indicated the slow initiation.
Fig. 2 SEC curves for chain extension of poly(β-myrcene). The black curve indicates the 1st batch of poly(β-myrcene) and the dotted curve indicates after polymerization of a 2nd portion of β-myrcene. |
Evidence of living behavior was also demonstrated by the synthesis of a well-defined poly(β-myrcene)-block-poly(isoprene) block copolymer by sequential introduction of β-myrcene and isoprene to the initiator/catalyst generated from [Nd(μ-DEP)3]x and TIBA with a molar ratio of [β-myrcene]:[isoprene]:[[Nd(μ-DEP)3]x]:[TIBA] = 150:300:1:30. The first block, poly(β-myrcene), was synthesized to generate a polymer with Mn = 6350 g mol−1 and PDI = 2.29. After complete consumption of β-myrcene, 300 equivalents of isoprene were introduced to generate the second block of the polymer with Mn = 15530 and PDI = 3.13. The 1H NMR spectrum of poly(β-myrcene)-block-poly(isoprene) copolymer is shown in Fig. 3a and estimated to contain the composition of 25 mol% of poly(β-myrcene) and 75 mol% of poly(isoprene). The SEC traces of the polymer both before and after the addition of the second monomer are both monomodal (Fig. 3b). Thus, we can claim that a single polymer product was produced rather than a mixture of two separate polymer populations.
Further livingness behavior was demonstrated by the successful synthesis of block copolymer poly(β-myrcene)-b-poly(isoprene). These results are unusual for a halide-free system, as halides are generally required for good performance in these Ziegler-Natta type catalytic systems. These results show that this is not strictly the case and suggest that worthwhile catalytic systems can be found in compositions that previously would not have been considered.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c8ra10050k |
This journal is © The Royal Society of Chemistry 2019 |