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Article

Non-Symmetrically Fused Bis(arylimino)pyridines with para-Phenyl Substitution: Exploring Their Use as N′,N,N″-Supports in Iron Ethylene Polymerization Catalysis

by
Yizhou Wang
1,2,
Zheng Wang
1,3,
Qiuyue Zhang
1,
Yanping Ma
1,
Gregory A. Solan
1,4,*,
Yang Sun
1 and
Wen-Hua Sun
1,2,*
1
Key Laboratory of Engineering Plastics, Beijing National Laboratory for Molecular Sciences, Institute of Chemistry Chinese Academy of Sciences, Beijing 100190, China
2
CAS Research/Education Center for Excellence in Molecular Sciences, University of Chinese Academy of Sciences, Beijing 100049, China
3
College of Science, Hebei Agricultural University, Baoding 071001, China
4
Department of Chemistry, University of Leicester, University Road, Leicester LE1 7RH, UK
*
Authors to whom correspondence should be addressed.
Catalysts 2024, 14(3), 213; https://doi.org/10.3390/catal14030213
Submission received: 4 February 2024 / Revised: 9 March 2024 / Accepted: 18 March 2024 / Published: 21 March 2024
(This article belongs to the Special Issue State of the Art in Molecular Catalysis in Europe)
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Versions Notes

Abstract

:
Through the implementation of a one-pot strategy, five examples of non-symmetrical [N,N-diaryl-11-phenyl-1,2,3,7,8,9,10-heptahydrocyclohepta[b]quinoline-4,6-diimine]iron(II) chloride complexes (aryl = 2,6-Me2Ph Fe1, 2,6-Et2Ph Fe2, 2,6-i-Pr2Ph Fe3, 2,4,6-Me3Ph Fe4, and 2,6-Et2-4-MePh Fe5), incorporating fused six- and seven-membered carbocyclic rings and appended with a remote para-phenyl group, were readily prepared. The molecular structures of Fe2 and Fe3 emphasize the variation in fused ring size and the skewed disposition of the para-phenyl group present in the N′,N,N″-ligand support. Upon activation with MAO or MMAO, Fe1–Fe5 all showed high catalytic activity for ethylene polymerization, with an exceptional level of 35.92 × 106 g (PE) mol−1 (Fe) h−1 seen for mesityl-substituted Fe4/MMAO operating at 60 °C. All catalysts generated highly linear polyethylene with good control of the polymer molecular weight achievable via straightforward manipulation of run temperature. Typically, low molecular weight polymers with narrow dispersity (Mw/Mn = 1.5) were produced at 80 °C (MMAO: 3.7 kg mol−1 and MAO: 4.9 kg mol−1), while at temperatures between 40 °C and 50 °C, moderate molecular weight polymers were obtained (MMAO: 35.6–51.6 kg mol−1 and MAO: 72.4–95.5 kg mol−1). Moreover, analysis of these polyethylenes by 1H and 13C NMR spectroscopy highlighted the role played by both β-H elimination and chain transfer to aluminum during chain termination, with the highest rate of β-H elimination seen at 60 °C for the MMAO-activated system and 70 °C for the MAO system.

1. Introduction

Remarkable advances have been made in the design of iron and cobalt catalysts for olefin oligomerization and polymerization ever since the first disclosures in the late 1990s [1,2,3,4], which reflect the vital function played by the metal–ligand complex. With particular regard to the ligand, N,N,N-chelating 2,6-bis(arylimino)pyridines (A, Figure 1) have paved the way with a host of structural modifications reported over the last two and a half decades or so, culminating in notable effects on polymer structure and catalytic activity [5,6,7,8,9,10,11]. From an industrial perspective, 2-imino-1,10-phenanthroline complexes (B, Figure 1) have shown the greatest promise with a successful pilot-scale process for making linear α-olefins using iron derivatives now being scaled up into a 200,000-ton process in China (in construction since November 2021) [12,13,14].
Elsewhere, the fusion of carbocyclic groups to the central pyridine in A has provided an effective means to not only enhance the thermostability and activity of the iron or cobalt catalyst [15,16,17,18,19,20,21,22,23,24] but also impart significant effects on the polymer products and catalytic activity. For example, cobalt-containing Cn=1 (R = Me, Figure 1) incorporating a single six-membered fused ring [17] exhibited high activity for ethylene polymerization and, indeed, superior thermal stability to the prototypical cobalt catalyst A [1,2]. Similarly, iron and cobalt complexes containing a larger fused seven-membered ring, Cn=2 (R = Ph, Figure 1) [18], showed improved thermal stability as well as a good catalytic lifetime. By contrast, doubly fused D2(n=1)-type iron and cobalt complexes (Figure 1) [15], bearing two six-membered carbocyclic rings, have a tendency towards generating mixtures of oligomers and polyethylenes that limit their usefulness. However, this limitation can be overcome by increasing the ring size of the two fused rings, with the seven-membered ring-containing iron complex D2(n=2) (Figure 1) [20], affording uniquely polyethylene. Furthermore, the bis(eight-membered) iron examples of D2(n=3) (Figure 1) afford higher molecular weight polymer with very high activity (up to 1.2 × 107 g (PE) mol−1 (Fe) h−1) [17,22].
As a result of this fused ring strategy, bis(imino)pyridine complexes integrated with carbocyclic rings of different ring sizes have also started to emerge. For instance, En=1/n=2-type cobalt complexes (Figure 1) [23], containing both six- and seven-membered carbocycles, allow access to low molecular-weight vinyl-terminated polyethylenes (Mw range: 1.5–22.8 kg mol−1) with extremely narrow dispersity (Mw/Mn range: 1.5–2.1), materials that have received some attention as functional polymers for use in copolymerization [25,26,27]. In pursuit of better catalytic performance, iron examples of En=1/n=2 have been shown to exhibit very high activity with levels reaching up to 1.6 × 107 g (PE) mol−1 (Fe) h−1 at 40 °C forming bimodal polyethylenes [24].
As an alternative direction in N,N,N ligand design, the introduction of hydrocarbyl groups (e.g., CH2CH2Ph, CH2Ph, and CH2CH=CH2) to the para-position of the central pyridine in A has seen reports of iron and cobalt catalysts (F, Figure 1) that can influence molecular weight as well as the dispersity of the resulting polyethylene [28]. More recently, the introduction of a para-phenyl group to the central pyridine in cobalt-containing En=1/n=2 to form G (Figure 1) has also seen unexpected enhancement effects on catalytic activity and molecular weight [29].
Given the superior catalytic performance generally seen for iron over cobalt in ethylene polymerization, we now target a series of para-phenyl-substituted ferrous examples of type G (Figure 1). In particular, five examples are disclosed that differ in the steric and electronic properties of the two N-aryl groups. To explore their use as catalysts in ethylene polymerization, a comprehensive evaluation has been undertaken that probes the type of aluminum alkyl activator as well as the effect of run temperature, Al:Fe molar ratio, reaction time, and ethylene pressure. To shed some light on any effects imparted by the para-phenyl group in the polymerizations, comparisons are made throughout with structurally related doubly fused iron catalysts such as D and E (Figure 1). Besides this polymerization study, the synthetic details and characterization of all five iron(II) complexes are also presented.

2. Results and Discussion

2.1. Synthesis and Characterization of Fe1–Fe5

To access the [N,N-diaryl-11-phenyl-1,2,3,7,8,9,10-heptahydrocyclohepta[b]quinoline-4,6-diimine]iron(II) chloride complexes (aryl = 2,6-Me2Ph Fe1, 2,6-Et2Ph Fe2, 2,6-i-Pr2Ph Fe3, 2,4,6-Me3Ph Fe4, and 2,6-Et2-4-MePh Fe5), a straightforward one-pot approach proved effective. Specifically, by reacting 11-phenyl-1,2,3,7,8,9,10-heptahydrocyclohepta[b]quinoline-4,6-dione [24,29,30], the corresponding aniline and iron(II) chloride tetrahydrate in n-butanol at reflux under an atmosphere of nitrogen, in the presence of acetic acid as catalyst, Fe1–Fe5 could be prepared as blue solids in yields of between 37% and 87% (Scheme 1). Attempts to make these complexes in a stepwise manner via the free ligand were hampered by difficulties in the purification of the diimine ligand due, in part, to the enamine tautomerism observed [15,24,31]. All five iron complexes proved stable when left to stand in the open air, but in solution, some evidence for oxidation could be detected. The characterization of these complexes was achieved using FT-IR spectroscopy, ESI mass spectrometry, and elemental analysis, while the crystals of Fe2 and Fe3 have been the subject of single X-ray diffraction studies.
Single crystals of Fe2 and Fe3 suitable for the X-ray determinations were grown in the glovebox under a nitrogen atmosphere by the slow diffusion of diethyl ether into a dichloromethane solution of the corresponding complex at ambient temperature. Perspective views of Fe2 and Fe3 are displayed in Figure 2 and Figure 3; selected bond lengths and bond angles are presented in Table 1. For Fe3, the six- and seven-membered fused rings were disordered across both carbocyclic positions, an observation that has been noted previously [29]. Each structure consists of a single iron center coordinated by a tridentate N,N-diaryl-11-phenyl-1,2,3,7,8,9,10-heptahydrocyclohepta[b]quinoline-4,6-diimine ligand (aryl = 2,6-diethylphenyl Fe2, 2,6-diisopropylphenyl Fe3) and two chlorides to form a five-coordinate geometry, which can be best regarded as a distorted square pyramidal with Cl2 occupying the apex and the three nitrogen atoms and Cl1 the base. Some level of quantification of the degree of distortion can be demonstrated by using the tau value (τ), where τ = 0 represents an ideal square pyramidal and τ = 1 is an ideal trigonal bipyramid [32]. For Fe2 and Fe3, τ = 0.11 and 0.21, respectively, which points towards modest distortions from an ideal square pyramidal, with the more sterically hindered 2,6-diisopropyl-containing Fe3 causing a slightly larger distortion than in Fe2. The iron atom itself in each structure sits at a distance of 0.576 Å above the N1–N2–N3–Cl1 basal plane in Fe2 and 0.536 Å in Fe3.
With regard to N′,N,N″–Fe chelation, the Fe–N distance involving the central Fe-Npyridine bond is the shortest (Fe1–N2: 2.142(5) Å Fe2, 2.076(3) Å Fe3), as is typical of previous analogs and reflects the binding properties of the tridentate ligand [20,22,24]. For the longer exterior Fe–Nimino bonds, some variation is evident between structure and those in Fe2 comparable (2.241(5) and 2.240(5) Å), while in Fe3 the Fe1–N1 distance (2.228(2) Å) is noticeably longer than the Fe1–N3 one (2.169(3) Å), likely reflecting the steric properties of the larger 7-membered carbocycle and the bulky ortho-isopropyl groups. Notably, in the non-phenyl substituted iron(II) counterpart of Fe3, E (M = Fe, Ar = diisopropylphenyl, Figure 1), the exterior Fe–Nimine distances are equivalent (2.216(1) Å) [24], which suggests the para-phenyl group in Fe3 exerts some long-range influence on the binding properties of this particular N′,N,N″-ligand. On the other hand, a similar comparison of the Fe–Npyridine bond distance in Fe3 with that in E (M = Fe, Ar = diisopropylphenyl, Figure 1) shows only a modest lengthening in the former (2.076(3) vs. 2.060(1) Å). For both Fe2 and Fe3, some deviation from coplanarity between the exterior imine groups and pyridine ring is seen, as is evidenced by the N2–C1–C2–N1 torsion angles (11.82° Fe2, 11.40° Fe3) and N2–C14–C13–N3 (8.12° Fe2, 10.90° Fe3), which can be credited to the strain imparted by the carbocyclic groups on the N′,N,N″-ligand framework.
As is common to many bis(arylimino)pyridine-iron complexes, the two N-aryl groups are inclined essentially perpendicularly to the N′,N,N″-coordination plane in both Fe2 and Fe3, thereby positioning the ortho-substituents above and below this plane. The six- and seven-membered carbocycles in the chelating ligand adopt puckered arrangements, with the latter showing the most flexibility. The para-phenyl groups themselves in Fe2 and Fe3 adopt skewed dispositions with respect to the neighboring pyridine plane (tors. C9–C8–C15–C20 84.66° Fe2, 56.16° Fe3) due to the rotary flexibility of the para-phenyl group; similar flexibility has been noted in their cobalt analogs [29]. There are no intermolecular contacts of note.
In the FT-IR spectra of Fe1–Fe5 (Figures S14–S18), characteristic peaks were identifiable for the imine double bonds between 1604 and 1617 cm−1, a range that is quite typical for coordinated imine groups in related iron(II) complexes [20,22,24,33,34]. In addition, the microanalytical data for each iron complex lend good support for compositions of the type LFeCl2.

2.2. Ethylene Polymerization Investigations Using Fe1–Fe5

As has been noted previously, methylaluminoxane (MAO) and modified methylaluminoxane (MMAO) are among the most effective activators for iron-based ethylene polymerization catalysis [20,22,24]. Accordingly, these two aluminoxanes were taken forward as part of parallel studies with the purpose of exploring not only structure–activity/polymer correlations in Fe1–Fe5 but also the impact of the type of activator on these correlations. All polymerizations were conducted in toluene, with the ethylene pressure initially set at 10 atm.

2.2.1. Polymerization Studies Using Fe1–Fe5 under Activation with MMAO

To allow a workable set of polymerization conditions using MMAO, Fe4 was initially employed as the test precatalyst, and the most effective conditions identified were then extended to evaluate Fe1–Fe3 and Fe5; the complete set of results is shown in Table 2.
To examine the effect of run temperature, the polymerizations using Fe4/MMAO were initially carried out at temperatures between 40 °C and 80 °C with the Al:Fe molar ratio fixed at 2500:1 (Fe4: 1 μmol) and a run time of 30 min (entries 1–5, Table 2). Inspection of the results reveals the catalytic activity reached a maximum of 19.14 × 106 g (PE) mol−1 (Fe) h−1 at 60 °C and still remained high with the temperature at 80 °C, with a level of 7.32 × 106 g (PE) mol−1 (Fe) h−1 noted (Figure 4). These performance characteristics reflect the appreciable thermal stability of Fe4. With regard to the polymer generated, the GPC traces indicate that the molecular weight rapidly decreased from 51.6 kg mol−1 to 3.7 kg mol−1 as the temperature was increased from 40 °C to 80 °C, respectively, in line with the higher rate of chain termination at higher temperatures [24]. Furthermore, the dispersity of the polymer generated significantly narrowed as the temperature was increased (Mw/Mn: from 14.2 to 1.5), with an initially bimodal distribution becoming unimodal at temperatures in excess of 60 °C. This evidence of bimodality at lower temperatures could be attributed to the different chain transfer pathways operational, namely β-H elimination and chain transfer to aluminum alkyl species (e.g., AlMe3) in MMAO [4,10,24]. Alternatively, the bimodality could be caused by the presence of oxidized iron complexes, leading to additional active centers [22]. On the other hand, at higher run temperatures, it would seem plausible that either a single active center predominates or a single chain transfer pathway becomes prevalent [22].
Thereafter, the polymerizations using Fe4/MMAO were undertaken at Al:Fe molar ratios between 1500:1 and 2500:1, with the temperature kept at 60 °C (entries 3 and 6–9, Table 2). As can be seen from the tabulated results, the highest activity of 34.10 × 106 g (PE) mol−1 (Fe) h−1 was recorded with the ratio at 2000:1, which was extremely high when compared with previously reported N,N,N-iron catalysts under comparable reaction conditions [20,22,24]. With the Al:Fe molar ratio gradually increasing from 1500:1 to 2500:1, the highest molecular weight polymer of 85.1 kg mol−1 was recorded at 2250:1, while the lowest of 9.8 kg mol−1 was obtained at 2500:1 (Figure 5). This dramatic decline in molecular weight with ratios exceeding 2250:1 reflects the critical value of aluminoxane necessary before chain transfer from the active species to aluminum in MMAO becomes significant [22,24].
To explore the effect of the run time using Fe4/MMAO, five separate polymerizations were conducted over 5, 15, 30, 45, and 60 min with the Al:Fe molar ratio kept at 2000:1 and the temperature at 60 °C (entries 8 and 10–13, Table 2). As time elapsed, the activity rapidly decreased from 97.44 × 106 g (PE) mol−1 (Fe) h−1 after 5 min to 18.24 × 106 g (PE) mol−1 (Fe) h−1 by the one-hour mark (Figure 6), suggesting a short induction period for this catalyst and a relatively long lifetime for the active species [20,22,24]. With respect to the molecular weight data, a gradual increase was observed in the first 15 min, followed by a rapid increase between 15 and 30 min, and then assuming a more constant level of molecular weight as the run reached 60 min. In terms of the dispersity, a steady increase was noted over the first 15 min (Mw/Mn: from 3.5 to 3.9) before a significant broadening and the onset of some bimodality were seen between 30 and 60 min (Mw/Mn: from 9.1 to 9.6), suggesting the formation of another active species [22] or an additional chain transfer pathway becoming operative.
To investigate the effect of the ethylene pressure on the polymerizations using Fe4/MMAO, the runs were additionally conducted at pressures of 1 and 5 atm with the Al:Fe molar ratio fixed at 2000:1 and the temperature kept at 60 °C (entries 8, 14, and 15, Table 2). At 1 atm, the lowest activity of 1.22 × 106 g (PE) mol−1 (Fe) h−1 was observed, which can be credited to the relatively low solubility of ethylene in toluene at this pressure [24]. On the other hand, at 10 atm, the activity attained its highest value (34.10 × 106 g (PE) mol−1 (Fe) h−1) and indeed was around twice that seen at 5 atm (17.96 × 106 g (PE) mol−1 (Fe) h−1), underscoring the beneficial effect of ethylene pressure on productivity.
On the strength of the most effective set of conditions identified using Fe4/MMAO (run temperature = 60 °C, Al:Fe = 2000:1, run time = 30 min, PC2H4 = 10 atm), the remaining iron precatalysts, Fe1, Fe2, Fe3, and Fe5, were then studied accordingly (entries 16–19, Table 2). All catalysts displayed high activity (range: 7.64–34.10 × 106 g (PE) mol−1 (Fe) h−1), with the relative order being: Fe4 (2,4,6-trimethyl) > Fe2 (2,6-diethyl) > Fe1 (2,6-dimethyl) > Fe3 (2,6-diisopropyl) > Fe5 (2,6-diethyl-4-methyl) (Figure 7). These results suggest that less bulky ortho-R1 groups are, in general, beneficial to the process of ethylene coordination/migratory insertion [24,30,35]. Nevertheless, it is evident that there are some anomalies in this structure/activity correlation, which could be attributable to the long-range effect of the para-phenyl group on carbocyclic ring flexibility and, in turn, N-aryl group binding/inclination [29].
As for the GPC traces, moderate molecular weight polymer (Mw: 26.4–81.3 kg mol−1) was obtained for all precatalysts, while the dispersities were in all cases broad (Mw/Mn: 6.4–13.6). Indeed, the least hindered Fe4-formed polymer exhibited a higher molecular weight than that seen for diisopropyl-containing Fe3, which was quite different from previous studies where larger ortho-substituents tend to promote higher molecular weight material [20,22,24]. The reason for this observation remains uncertain but may conceivably be attributed to the para-phenyl group somehow influencing chain propagation, which is most apparent in the more sterically hindered Fe3. By contrast, the less bulky Fe1 (2,6-dimethyl) and Fe2 (2,6-diethyl) are less affected by the para-phenyl group, resulting in the molecular weight of the polymer formed by Fe2 being greater than that of Fe1, an observation that can be credited to the bulkier ortho-ethyl groups better protecting the active center [20,22,24].
To understand the performance characteristics of the current catalysts in terms of activity and polymer molecular weight and dispersity, data for mesityl-containing Fe4 (denoted in G as in Figure 1) are collected in Figure 8 alongside that for some previously reported iron systems incorporating doubly fused carbocycles. From this bar chart, it is evident that the highest activity of these iron complexes follows the order: G (Fe4: this work) >> En=1/n=2 > D2(n=3) ≈ D2(n=2) (Figure 1) [20,22,24]. Evidently, the para-phenyl group in G exerts a positive effect on catalytic activity, which is most striking when compared to its non-phenyl substituted comparator En=1/n=2, a finding that mirrors that seen with the cobalt counterparts [29]. While the origin of the effect remains uncertain, we consider the para-phenyl group to have a limited effect on the binding properties of this mesityl-substituted N′,N,N″-ligand. Indeed, analysis of the X-ray structure of the 2,6-diethylphenyl-containing Fe2 showed no evidence of uneven binding of the chelating ligand, a feature that was notably apparent in the bulkier derivative Fe3 (see above). One plausible explanation for G (Fe4) being more active than En=1/n=2 stems from the electron-withdrawing properties of the phenyl group and the impact this has on the ethylene coordination and insertion at the active iron center. Furthermore, the molecular weight of the polyethylene decreases in the following order: D2(n=3) > G (Fe4: this work) > E n=1/n=2 > D2(n=2). This finding shows that the presence of both the large eight-membered fused structure (D2(n=3)) and the para-phenyl group in G (Fe4) can have a favorable effect on the molecular weight of the polymer, observations that are similar to those observed for their cobalt analogs. In short, the introduction of the para-phenyl group to the N′,N,N″-ligand periphery in G has the effect of promoting the catalytic activity and increasing the molecular weight of the polymer for both iron and cobalt complexes. In terms of the optimal run temperature, G (Fe4: this work) proved the most effective by operating effectively at 60 °C, which compares to 40 °C for the non-para-phenyl substituted analog En=1/n=2 [24], a result that suggests the para-phenyl group can also help provide a more stable active species at higher operating temperatures. As a final point, it can be seen from the figure that the dispersity is broad for all of these iron complexes, in line with the different chain transfer pathways that are operational.

2.2.2. Polymerization Studies Using Fe1–Fe5 under Activation with MAO

To enable a comparison with the polymerization runs performed with MMAO, MAO was also employed in the activation of Fe1–Fe5. As before, Fe4 was initially employed as the test precatalyst so as to identify an effective set of reaction conditions that could be used to screen the other iron precatalysts (Table 3).
In the first instance, the polymerization runs were performed using Fe4/MAO at run temperatures of between 40 and 80 °C (entries 1–5, Table 3) with the Al:Fe molar ratio fixed at 2500:1 and the run time at 30 min (entries 1–5, Table 3). The highest catalytic activity of 30.58 × 106 g (PE) mol−1 (Fe) h−1 was achieved at 60 °C, reflecting the outstanding thermal stability of this iron catalyst. Moreover, the molecular weight of the polymer dropped rapidly from 95.5 kg mol−1 at 40 °C to 4.9 kg mol−1 at 80 °C (Figure S1), which can be attributed to the higher rate of chain transfer at high temperatures [24]. As for the polymer dispersity, this decreased from 18.5 (40 °C) to 1.5 (80 °C) as the temperature increased, which manifests itself in the initially bimodal distribution becoming unimodal, findings that likely stem from the two chain transfer pathways becoming less competitive at higher temperatures [9,10,36].
Following this, the polymerizations were evaluated with Al:Fe molar ratios of 1000:1, 1500:1, 2000:1, 2500:1, and 3000:1 with the temperature fixed at 60 °C (entries 3 and 6–9, Table 3). As a result, the highest activity of 35.92 × 106 g (PE) mol−1 (Fe) h−1 was noted with the ratio of 2000:1 (Figure S2), which was marginally higher than the optimal activity for the MMAO runs (34.10 × 106 g (PE) mol−1 (Fe) h−1). As for the molecular weight of the polymer, this was found to markedly decrease from 161.2 to 32.3 kg mol−1 as the Al:Fe molar ratio was increased, in line with a higher rate of chain transfer [24].
To shed light on the catalytic lifetime of the active center in Fe4/MAO, the polymerizations were carried out at different run times with the temperature and Al:Fe molar ratio kept at 60 °C and 2000:1, respectively. As expected, an exceptionally high activity of 84.96 × 106 g (PE) mol−1 (Fe) h−1 was observed after 5 min (entry 10, Table 3), which then progressively decreased to 18.65 × 106 g (PE) mol−1 (Fe) h−1 at 60 min (entry 13, Table 3), suggesting a short induction period and an excellent lifetime for the active center [20]. Meanwhile, the molecular weight of the polyethylene increased from 16.8 to 168.0 kg mol−1 over time (Figure S3), while the dispersity (Mw/Mn) increased from 3.8 to 16.6 in a similar manner to that seen for Fe4/MMAO.
On lowering the ethylene pressure from 10 atm to 1 atm using Fe4/MAO, a sharp decline in activity was observed from 35.92 × 106 g (PE) mol−1 (Fe) h−1 to 0.84 × 106 g (PE) mol−1 (Fe) h−1 (entries 8, 14, and 15, Table 3), which most likely derives from the lower solubility of ethylene in toluene at lower pressure [23,29]. Furthermore, the molecular weight of the polyethylene decreased noticeably from 129.0 to 3.4 kg mol−1 by dropping the pressure from 10 atm to 1 atm, an observation that supports the lower rates of chain propagation that are operational at lower pressure [24]. In addition, the molecular weight of the polyethylene formed during the Fe4/MAO runs was higher than that seen using Fe4/MMAO, reflecting the lower rate of chain transfer with MAO.
To gain further insight into the role of the N-aryl variations in Fe1–Fe5, the optimal conditions identified using Fe4/MAO (namely reaction temperature of 60 °C, Al:Fe molar ratio of 2000:1, ethylene pressure of 10 atm, and run time of 30 min) were deployed to evaluate the other iron precatalysts, Fe1–Fe3 and Fe5 (entries 16–19, Table 3). All iron complexes exhibited high activity (range: 13.04–35.92 × 106 g (PE) mol−1 (Fe) h−1) and produced highly linear polyethylenes (Tm: 131–133 °C) with broad dispersities. On analysis of their relative performance, the catalytic activity decreased in the following order: Fe4 (aryl = 2,4,6-trimethylphenyl) > Fe1 (aryl = 2,6-dimethylphenyl) > Fe2 (aryl = 2,6-diethylphenyl) > Fe5 (aryl = 2,6-diethyl-4-methylphenyl) > Fe3 (aryl = 2,6-diisopropylphenyl) (Figure S4). As is evident, the precatalysts bearing the least bulky substituents in the ortho positions of the N-aryl groups, Fe4 and Fe1, exhibited higher activity due to the faster rates of ethylene insertion and chain propagation [24,30,35]. Moreover, mesityl-containing Fe4 produced the highest molecular weight polyethylene of the series, which was also seen for the MMAO runs, but nonetheless unexpected when compared with previous work in which the most sterically hindered complex usually affords the highest molecular weight polymer. This unusual finding plausibly arose from the very high activity seen for Fe4, thereby inhibiting chain transfer.

2.3. Structural Analysis of the Polyethylene

The microstructural characteristics of polymers are of great significance to their mechanical properties and, in turn, their processing ability. As has already been highlighted, the DSC thermograms for the polyethylenes produced in this work typically display Tm values of >130 °C in accordance with highly linear polymers (see Table 2 and Table 3) [16,18,20,23,24]. To obtain more information, selected polyethylene samples were further analyzed by 1H and 13C NMR spectroscopy with a view to understanding how run temperature and the type of aluminum activator impact the microstructure.
To begin with, we looked at the polymers generated using Fe4/MMAO at run temperatures of 40, 50, 60, 70, and 80 °C, where variations in molecular weight and dispersity were observed. To engender suitable solubility, these polymer samples were dissolved in the 1,1,2,2-tetrachloroethane-d2 at 100 °C, and their 1H NMR spectra were recorded at a similar temperature (entries 1–5, Table 2). For the 1H NMR spectrum of the polyethylene obtained using Fe4/MMAO at 80 °C (entry 5, Table 2: Mw = 3.7 kg mol−1, Mw/Mn = 1.5), a high-intensity resonance at δ 1.32 ppm for the –(CH2)n– repeat unit confirms the strictly linear nature of the polyethylene (Figure 9). Either side of this signal shows lower intensity peaks, which correspond to an n-propyl group (Hf, He, and Hd), while the more downfield region reveals multiplet peaks at δ 5.00 and 5.85 ppm, which can be assigned to a vinyl end-group (Ha and Hb). Evidently, the latter observation highlights the involvement of β-H elimination to metal or monomer during chain termination [24]. Moreover, by considering the integral ratio of vinyl Hb to methyl chain-end Hf (1/18.82) [29,37,38], the molar ratio of the unsaturated polymer chain to the saturated polymer chain can be determined as 0.379 (see SI), a value that implies the additional presence of a fully saturated polymer in line with chain transfer to aluminum being also operational [4,5]. Further support for these assignments was provided by the 13C NMR spectrum, which reveals a high-intensity peak around δ 29.43 ppm, which corresponds to the –(CH2)n– repeat unit, along with lower intensity peaks at δ 13.72, 22.38, and 31.66 ppm for an n-propyl end-group and weaker downfield peaks at δ 113.85 and 138.78 ppm for a terminal vinyl group (Figure 10) [24]. The absence of resonances corresponding to an isobutyl end-group rules out any chain transfer to aluminum-isobutyl species present within MMAO [30], which suggests that chain transfer to aluminum occurs solely with aluminum-methyl species.
The 1H NMR spectra for the polymers produced using Fe4/MMAO at the lower run temperatures (40–70 °C, entries 1–4, Table 2) revealed similar features, with signals characteristic of the -(CH2)n- repeat unit and weaker peaks for the n-propyl and vinyl chain-ends (Figures S5–S8). However, the molar ratio of unsaturated to saturated polymer chains showed some notable variations, with the value reaching a maximum of 1.98 at 60 °C (Figure 11), which implies that β-H elimination assumes the main chain termination pathway at this point. However, at temperatures below 60 °C, the ratio drops to 0.394 (50 °C) and then 0.108 (40 °C), reflecting the importance of chain transfer to aluminum-methyl species in MMAO at these temperatures. Evidently, the chain transfer pathways are affected by the run temperature, with the highest rate of β-H elimination occurring at 60 °C, which also corresponds to the optimal temperature in terms of catalytic activity.
To appreciate the effect of the aluminum activator on these chain transfer pathways, the polyethylenes produced using Fe4/MAO over the same run temperature range (40–80 °C) as that used for Fe4/MMAO were similarly investigated by 1H NMR spectroscopy. Once again, the 1H NMR spectra of all five polymer samples revealed peaks characteristic of a highly linear polymer backbone along with varying amounts of chain end vinyl and n-propyl groups (Figures S9–S13). Interestingly, the highest rate of β-H elimination using Fe4/MAO was found at 70 °C (Figure 12), as evidenced by the highest molar ratio of unsaturated to saturated polymer chains in the polymer (1.05: Hb:Hf = 1/8.71). Nevertheless, this value was lower than that seen with the MMAO-activated system, an observation that reflects the differences in the type of aluminoxane and their impact on the competing chain transfer pathways.

3. Materials and Methods

3.1. General Considerations

All operations making use of moisture and/or air-sensitive compounds were conducted under a nitrogen atmosphere by using standard Schlenk techniques or in a nitrogen-filled glovebox. Toluene, the solvent used for the polymerization studies, was heated to reflux for more than 12 h over sodium benzophenone and distilled under nitrogen prior to use. The aluminum reagents, methylaluminoxane (MAO, 1.5 M in toluene) and modified methylaluminoxane (MMAO, 2.5 M in n-heptane, containing 20–25%Al(i-Bu)3), were purchased from Anhui Botai Electronic Materials Co. (Chuzhou, China), while high-purity ethylene was procured from Beijing Yanshan Petrochemical Co. (Beijing, China) and used as received. Other chemical reagents were purchased from Concord Technology Co., Ltd. (Tianjin, China), Macklin Biochemical Technology Co., Ltd. (Shanghai, China), and Innochem Technology Co., Ltd. (Beijing, China) and used as received: diethyl ether (GR., Concord, Tianjin, China), n-hexane (GR., Concord, Tianjin, China), glacial acetic acid (AR., Concord, Tianjin, China), n-butanol (AR., Concord, Tianjin, China), ferrous chloride tetrahydrate (98% purity, Macklin, Shanghai, China), anilines (99% purity, Innochem, Beijing, China). The samples for FT-IR analysis were placed directly on the ATR attachment plane and pressed with a flat nut, and the FT-IR spectra were recorded on a PerkinElmer System 2000 FT-IR spectrometer (PerkinElmer Scientific, Waltham, MA, USA). The elemental analyses were conducted using a Flash EA 1112 microanalyzer (Thermo Fisher Scientific, Waltham, MA, USA). The ESI mass spectra were recorded using a Bruker solariX instrument (Bruker Corporation, Billerica, MA, USA) (Acquisition Mode: Single MS; Polarity: Positive; Broadband Low Mass: 57.7 m/z; Acquired Scans: 20; Broadband High Mass: 1000.0 m/z). The melting points of the polyethylenes were determined on a PerkinElmer TA-Q2000 DSC analyzer (PerkinElmer Scientific, Waltham, MA, USA) under a nitrogen atmosphere according to the following procedure: around 5.0 mg of the polymer was heated to 160 °C at a rate of 20 °C min−1 and then maintained for 3 min at 160 °C to remove the thermal history. After cooling to −20 °C at a rate of 20 °C min−1, the sample was then heated to 160 °C again at the rate of 10 °C min−1. The polymer molecular weight (Mw) and dispersity (Mw/Mn) were measured using an Agilent PLGPC 220GPC system running (Agilent Technologies Inc., Santa Clara, CA, USA) at 150 °C using 1,2,4-trichlorobenzene as the mobile phase; sample preparation involved agitation of ca. 10 mg of the polyethylene sample in 1,2,4-trichlorobenzene (5 mL) at 170 °C for more than 8 h to allow dissolution. The 1H NMR and 13C NMR spectra of the polymers were measured at 100 °C using a Bruker AVANVE 500 MHz instrument (Bruker Corporation, Billerica, MA, USA); sample preparation involved dissolving the selected polyethylene (ca. 50 mg) in 1,1,2,2-tetrachloroethane-d2 (0.6 mL), containing TMS as the internal standard, at 110 °C for more than 2 h. The 11-phenyl-1,2,3,7,8,9,10-heptahydrocyclohepta[b]quinoline-4,6-dione was prepared according to procedures reported elsewhere [29,39,40,41].

3.2. Synthesis of [N,N-diaryl-11-phenyl-1,2,3,7,8,9,10-heptahydrocyclohepta[b]quinoline-4,6-diimine]iron(II) Chloride (Fe1–Fe5)

3.2.1. Aryl = 2,6-Dimethylphenyl (Fe1)

Under an atmosphere of nitrogen, a mixture of 11-phenyl-1,2,3,7,8,9,10-heptahydrocyclohepta[b]quinoline-4,6-dione (0.153 g, 0.50 mmol), 2,6-dimethylaniline (0.242 g, 2.0 mmol), and ferrous chloride tetrahydrate (0.080 g, 0.40 mmol) was dissolved in n-butanol (2.0 mL), containing a catalytic amount of acetic acid (0.5 mL), and then stirred and heated to reflux for 2 h to give a blue-green solution. After cooling to room temperature, diethyl ether and n-hexane (32 mL, v:v = 1:1) were added to induce precipitation. This precipitate was then left to settle, and the supernatant solution was discarded. This process of adding diethyl ether/n-hexane (32 mL, v:v = 1:1) and discarding the supernatant solution was repeated two more times. Finally, the mixture was filtered and washed three times with diethyl ether and n-hexane (24 mL, v:v = 2:1), affording Fe1 as a blue powder (0.217, 85%). FT-IR (cm−1): 2950 (m), 1678 (m), 1617 (m, νC = N), 1570 (m), 1441 (s), 1376 (m), 1218 (s), 1073 (s), 920 (m), 844 (m), 770 (s), 704 (s). ESI-MS (m/z): Calculated for [C36H37ClFeN3]+ (602.20254). Found: 602.20232 (Figure S19). Elemental analysis: Calculated for C36H37Cl2N3Fe (638.46) C, 67.73, H, 5.84, N, 6.58. Found: C, 67.31, H, 6.25, N, 6.68%.

3.2.2. Aryl = 2,6-Diethylphenyl (Fe2)

By using a similar procedure to that outlined for Fe1, but with 2,6-diethylaniline as the arylamine, Fe2 was isolated as a blue powder (0.171 g, 66%). FT-IR (cm−1): 2965 (m), 2932 (m), 2870 (m), 1678 (m), 1613 (m, νC = N), 1567 (m), 1492 (m), 1447 (s), 1330 (m), 1216 (m), 1189 (m), 1106 (m), 1071 (m), 1030 (m), 951 (m), 848 (m), 809 (m), 776 (s), 703 (s). ESI-MS (m/z): Calculated for [C40H45ClFeN3]+ (658.26514). Found: 658.26496 (Figure S20). Elemental analysis: Calculated for C40H45Cl2N3Fe (694.57) C, 69.17, H, 6.53, N, 6.05. Found: C, 68.80, H, 6.71, N, 6.25%.

3.2.3. Aryl = 2,6-Diisopropylphenyl (Fe3)

By using a similar procedure to that outlined for Fe1, but with 2,6-diisopropylaniline as the arylamine, Fe3 was isolated as a blue powder (0.196 g, 65%). FT-IR (cm−1): 2962 (m), 2866 (m), 2361 (w), 1688 (w), 1611 (w, νC = N), 1568 (m), 1458 (s), 1383 (m), 1360 (m), 1324 (m), 1245 (m), 1214 (m), 1183 (m), 1124 (m), 1103 (m), 1051 (m), 943 (m), 848 (m), 804 (s), 774 (s), 709 (s). ESI-MS (m/z): Calculated for [C44H53ClFeN3]+ (714.32774). Found: 714.32762 (Figure S21). Elemental analysis: Calculated for C44H53Cl2N3Fe (750.67) C, 70.40, H, 7.12, N, 5.60. Found: C, 70.19, H, 7.42, N, 5.73%.

3.2.4. Aryl = 2,4,6-Trimethylphenyl (Fe4)

By using a similar procedure to that outlined for Fe1, but with 2,4,6-trimethylaniline as the arylamine, Fe4 was isolated as a blue powder (0.232 g, 87%). ESI-MS (m/z): Calculated for [C38H41ClFeN3]+ (630.23384). Found: 630.23370 (Figure S22). FT-IR (cm−1): 3336 (m), 2912 (s), 2108 (w), 1984 (w), 1683 (w), 1604 (w, νC = N), 1561 (m), 1472 (s), 1440 (s), 1376 (m), 1325 (m), 1215 (s), 1148 (m), 1071 (m), 1033 (m), 952 (w), 853 (s), 780 (w), 757 (w), 702 (s). Elemental analysis: Calculated for C38H41Cl2N3Fe (666.51) C, 68.84, H, 6.20, N, 6.30. Found: C, 68.71, H, 6.55, N, 6.17%.

3.2.5. Aryl = 2,6-Diethyl-4-methylphenyl (Fe5)

By using a similar procedure to that outlined for Fe1, but with 2,6-diethyl-4-methylaniline as the arylamine, Fe5 was isolated as a blue powder (0.106 g, 37%). ESI-MS (m/z): Calculated for [C42H49ClFeN3]+ (686.29644). Found: 686.29592 (Figure S23). FT-IR (cm−1): 3363 (m), 2964 (m), 2930 (m), 2870 (m), 1676 (w), 1612 (m, νC = N), 1566 (m), 1456 (s), 1373 (m), 1335 (m), 1257 (m), 1215 (m), 1150 (m), 1070 (m), 950 (m), 857 (s), 774 (m), 704 (s). Elemental analysis: Calculated for C42H49Cl2N3Fe (722.62) C, 69.81, H, 6.84, N, 5.82. Found: C, 69.57, H, 7.03, N, 5.61%.

3.3. Polymerization Studies

3.3.1. Ethylene Polymerization at 1 Atm Ethylene Pressure

A 250 mL Schlenk vessel, equipped with a stirrer bar, was loaded with Fe4 (0.7 mg, 1.0 μmol), and the vessel was subjected to three cycles of evacuation and back-filling with nitrogen before the atmosphere was replaced with ethylene (1 atm). Freshly distilled toluene (30 mL) was then injected to dissolve the iron complex, and the mixture was stirred and heated to 60 °C. The activator (MAO or MMAO) was immediately injected via a syringe, and the run commenced. After 30 min, the supply of ethylene was stopped and the pressure within the Schlenk flask vented. The reaction mixture was then quenched with 10% hydrochloric acid in ethanol (30 mL). The polymer was washed with ethanol and dried under reduced pressure at 100 °C until it reached a constant weight.

3.3.2. Ethylene Polymerization at 5 Atm or 10 Atm Ethylene Pressure

A 250 mL stainless steel autoclave, fitted with a mechanical stirrer, an ethylene pressure control device, and a temperature controller, was employed for the higher-pressure (5 atm or 10 atm) ethylene polymerization evaluations. The autoclave was evacuated and back-filled with high-purity nitrogen (2 cycles) and then pressurized with 5 atm of ethylene to check the gas tightness. With the ethylene pressure returning to 1 atm, the iron precatalyst (1.0 μmol), pre-mixed with toluene (25 mL) in a Schlenk tube, was immediately injected into the autoclave. Any remaining iron complex was washed into the autoclave with more toluene (25 mL), and then a further volume of toluene (25 mL) was added. The required amount of activator (MAO or MMAO) and additional toluene (25 mL) were injected successively into the autoclave to take the total volume of solvent to 100 mL. The ethylene pressure was then set at either 5 atm or 10 atm, and the stirring immediately commenced. After the requisite reaction time, the ethylene gas supplying the reactor was stopped, and the autoclave was allowed to cool to room temperature by surrounding it with an ice/water bath. The reactor was then slowly vented, and the contents of the autoclave were quenched with a 5% hydrochloric ethanol solution (50 mL). Finally, the polymer was filtered, washed three times with ethanol (30 mL), and dried under reduced pressure at 100 °C until it reached a constant weight.

3.4. Single Crystal X-ray Diffraction Studies

X-ray diffraction studies were conducted on Fe2 and Fe3, using single crystals of each iron complex that had been grown in the glove box by the slow diffusion of diethyl ether into a dichloromethane solution at ambient temperature. A crystal of each was selected and mounted on an XtaLAB Synergy R HyPix diffractometer (Rigaku Corporation, Tokyo, Japan) incorporating graphite-monochromated Cu-Kα radiation (λ = 1.54184 Å) at 170(2) K for Fe2 and 169.99(10) K for Fe3, and data collection commenced. Using Olex2, the structures were solved by employing the ShelXT structure solution program using intrinsic phasing and refined with the ShelXL refinement package using least squares minimization [42,43].

4. Conclusions

In summary, a straightforward one-pot strategy has been successfully implemented to prepare five examples of iron(II) chloride complexes, Fe1–Fe5, bearing bis(imino)pyridines fused with six- and seven-membered carbocyclic rings and further appended with a para-phenyl group. All these iron complexes have been characterized via FT-IR spectroscopy, ESI mass spectrometry, elemental analysis, and, in the cases of Fe2 and Fe3, by single crystal X-ray diffraction. On activation with MMAO or MAO, Fe1–Fe5 exhibited extremely high activity, with a maximum of 35.92 × 106 g (PE) mol−1 (Fe) h−1 seen for Fe4/MAO operating at 60 °C. All catalysts generated highly linear polymers with varying levels of vinyl end-groups that were dependent on run temperature. Interestingly, analysis of 1H NMR spectra of the polymers revealed higher rates of β-H elimination at 60 °C for the MMAO-activated system and 70 °C for the MAO-activated system, highlighting the key role played by temperature in influencing the competition between β-H elimination and chain transfer to aluminum. Moreover, considerable control of the polymer molecular weight could be achieved with Fe4 found to form low molecular weight polymer with narrow dispersity at high temperatures (70 or 80 °C), while higher molecular weight material was formed at lower run temperatures.
Perhaps more importantly, Fe4/MMAO exhibited outstanding thermal stability and was indeed superior to the non-phenyl substituted iron analog E/MMAO (Ar = 2,4,6-trimethlyphenyl, M = Fe, Scheme 1), which is evidenced by the optimal run temperature of Fe4/MMAO being 60 °C (cf. 40 °C for E/MMAO) and activity of 34.10 × 106 g (PE) mol−1 (Fe) h−1 (cf. 15.15 × 106 g (PE) mol−1 (Fe) h−1 for E/MMAO). Given the remoteness of the para-phenyl group from the active iron center, it would seem unlikely that it has a direct steric influence on the active site, though an indirect effect by impacting on the flexibility/steric properties of the neighboring fused carbocycles and, in turn, the binding properties of the N′,N,N″-ligand may be at play; an electronic effect cannot, however, be ruled out. More generally, these para-phenyl substituted carbocyclic-fused bis(imino)pyridine iron complexes exhibit excellent performance for ethylene polymerization when compared with a series of fused ring iron counterparts, including D2(n=2) and D2(n=3) (Figure 1), especially with respect to catalytic activity. As a similar effect on catalytic activity and molecular weight has been seen with their para-phenyl substituted cobalt counterparts (G, Figure 1), we aim in future work to further probe the generality of this structural variation in catalyst design.

Supplementary Materials

The following supporting information can be downloaded at: https://www.mdpi.com/article/10.3390/catal14030213/s1. Figure S1: (a) GPC traces for the polyethylenes generated using Fe4/MAO at different run temperatures and (b) plots of catalytic activity and polymer molecular weight as a function of run temperature; Figure S2: (a) GPC traces for the polyethylenes generated using Fe4/MAO at various Al:Fe molar ratios and (b) plots of catalytic activity and polymer molecular weight as a function of Al:Fe molar ratio; Figure S3: (a) GPC traces for the polyethylenes generated using Fe4/MAO over reaction time and (b) plots of catalytic activity and polymer molecular weight as a function of reaction time; Figure S4: (a) GPC traces for the polyethylenes generated using Fe1–Fe5 under MAO activation and (b) a bar chart showing the effects of variation in N-aryl group in Fe1–Fe5 on catalytic activity and polymer molecular weight; Figure S5: 1H NMR spectrum of the polyethylene produced using Fe4/MMAO operating at 70 °C (entry 4, Table 2); recorded at 100 °C in 1,1,2,2-tetrachloroethane-d2; Figure S6: 1H NMR spectrum of the polyethylene produced using Fe4/MMAO operating at 60 °C (entry 3, Table 2); recorded at 100 °C in 1,1,2,2-tetrachloroethane-d2; Figure S7: 1H NMR spectrum of the polyethylene produced using Fe4/MMAO operating at 50 °C (entry 2, Table 2); recorded at 100 °C in 1,1,2,2-tetrachloroethane-d2; Figure S8: 1H NMR spectrum of the polyethylene produced using Fe4/MMAO operating at 40 °C (entry 1, Table 2); recorded at 100 °C in 1,1,2,2-tetrachloroethane-d2; Figure S9: 1H NMR spectrum of the polyethylene produced using Fe4/MAO operating at 40 °C (entry 1, Table 3); recorded at 100 °C in 1,1,2,2-tetrachloroethane-d2; Figure S10: 1H NMR spectrum of the polyethylene produced using Fe4/MAO operating at 50 °C (entry 2, Table 3); recorded at 100 °C in 1,1,2,2-tetrachloroethane-d2; Figure S11: 1H NMR spectrum of the polyethylene produced using Fe4/MAO operating at 60 °C (entry 3, Table 3); recorded at 100 °C in 1,1,2,2-tetrachloroethane-d2; Figure S12: 1H NMR spectrum of the polyethylene produced using Fe4/MAO operating at 70 °C (entry 4, Table 3); recorded at 100 °C in 1,1,2,2-tetrachloroethane-d2; Figure S13: 1H NMR spectrum of the polyethylene produced using Fe4/MAO operating at 80 °C (entry 5, Table 3); recorded at 100 °C in 1,1,2,2-tetrachloroethane-d2; Table S1: Determining the molar ratios of a (chain A, unsaturated) to b (chain B, fully saturated) for the PE’s produced using Fe4/MMAO at various temperatures; Table S2: Determining the molar ratios of a (chain A, unsaturated) to b (chain B, fully saturated) for the PE’s produced using Fe4/MAO at various temperatures; Table S3: Crystal data and structure refinement for Fe2 and Fe3. Figure S14: FT-IR spectrum of Fe1. Figure S15: FT-IR spectrum of Fe2. Figure S16: FT-IR spectrum of Fe3. Figure S17: FT-IR spectrum of Fe4. Figure S18: FT-IR spectrum of Fe5. Figure S19: ESI-MS spectrum of Fe1. Figure S20: ESI-MS spectrum of Fe2. Figure S21: ESI-MS spectrum of Fe3. Figure S22: ESI-MS spectrum of Fe4. Figure S23: ESI-MS spectrum of Fe5. References [24,29,38,44] are cited in the Supplementary Materials.

Author Contributions

Y.W.: methodology, investigation, data curation, writing—original draft preparation, and writing—review and editing; Z.W.: methodology, validation, supervision, and writing—review and editing; Q.Z.: data curation; Y.M.: software; G.A.S.: visualization, writing—review and editing; Y.S.: X-ray diffraction; W.-H.S.: conceptualization, resources, supervision, funding acquisition, and writing—review and editing. All authors have read and agreed to the published version of the manuscript.

Funding

This research was funded by the National Natural Science Foundation of China (21871275).

Data Availability Statement

CCDC reference numbers 2325145–2325146 contain Supplementary crystallographic Information for Fe2 and Fe3, and the data presented in this study are available in this article.

Acknowledgments

G.A.S. thanks the Chinese Academy of Sciences for a President’s International Fellowship for Visiting Scientists.

Conflicts of Interest

The authors declare no conflicts of interest.

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Figure 1. Bis(arylimino)pyridine iron(II)/cobalt(II) chlorides, A, and some key variations made to the N,N,N-ligand skeleton in B–G.
Figure 1. Bis(arylimino)pyridine iron(II)/cobalt(II) chlorides, A, and some key variations made to the N,N,N-ligand skeleton in B–G.
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Scheme 1. One-pot route to Fe1–Fe5 from 11-phenyl-1,2,3,7,8,9,10-heptahydrocyclohepta[b]quinoline-4,6-dione.
Scheme 1. One-pot route to Fe1–Fe5 from 11-phenyl-1,2,3,7,8,9,10-heptahydrocyclohepta[b]quinoline-4,6-dione.
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Figure 2. ORTEP representation of Fe2 with the thermal ellipsoids shown at the 50% probability level; all the hydrogen atoms and solvents have been omitted for clarity.
Figure 2. ORTEP representation of Fe2 with the thermal ellipsoids shown at the 50% probability level; all the hydrogen atoms and solvents have been omitted for clarity.
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Figure 3. ORTEP representation of Fe3 with the thermal ellipsoids shown at the 50% probability level; all the hydrogen atoms have been omitted for clarity.
Figure 3. ORTEP representation of Fe3 with the thermal ellipsoids shown at the 50% probability level; all the hydrogen atoms have been omitted for clarity.
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Figure 4. (a) GPC traces of the polyethylenes generated using Fe4/MMAO at different temperatures and (b) plots of catalytic activity and polymer molecular weight as a function of run temperature.
Figure 4. (a) GPC traces of the polyethylenes generated using Fe4/MMAO at different temperatures and (b) plots of catalytic activity and polymer molecular weight as a function of run temperature.
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Figure 5. (a) GPC traces of the polyethylenes generated using Fe4/MMAO at various Al:Fe molar ratios and (b) plots of catalytic activity and polymer molecular weight as a function of Al:Fe molar ratio.
Figure 5. (a) GPC traces of the polyethylenes generated using Fe4/MMAO at various Al:Fe molar ratios and (b) plots of catalytic activity and polymer molecular weight as a function of Al:Fe molar ratio.
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Figure 6. (a) GPC traces of the polyethylenes generated using Fe4/MMAO as the run time was varied, and (b) plots of catalytic activity and polymer molecular weight as a function of reaction time.
Figure 6. (a) GPC traces of the polyethylenes generated using Fe4/MMAO as the run time was varied, and (b) plots of catalytic activity and polymer molecular weight as a function of reaction time.
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Figure 7. (a) GPC traces of the polyethylenes generated using Fe1–Fe5 with MMAO as an activator and (b) a bar chart showing catalytic activity and polymer molecular weight with respect to the iron precatalyst employed.
Figure 7. (a) GPC traces of the polyethylenes generated using Fe1–Fe5 with MMAO as an activator and (b) a bar chart showing catalytic activity and polymer molecular weight with respect to the iron precatalyst employed.
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Figure 8. Comparison of the catalytic activity, polymer molecular weight, and dispersity obtained using G (Fe4, this work) with that for carbocyclic-fused iron precatalysts, D2(n=2), D2(n=3), and E n=1/n=2; all polymerizations were conducted using MMAO at 10 atm of ethylene and under optimal reaction conditions.
Figure 8. Comparison of the catalytic activity, polymer molecular weight, and dispersity obtained using G (Fe4, this work) with that for carbocyclic-fused iron precatalysts, D2(n=2), D2(n=3), and E n=1/n=2; all polymerizations were conducted using MMAO at 10 atm of ethylene and under optimal reaction conditions.
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Figure 9. 1H NMR spectrum of the polyethylene produced using Fe4/MMAO operating at 80 °C (entry 5, Table 2); recorded at 100 °C in 1,1,2,2-tetrachloroethane-d2.
Figure 9. 1H NMR spectrum of the polyethylene produced using Fe4/MMAO operating at 80 °C (entry 5, Table 2); recorded at 100 °C in 1,1,2,2-tetrachloroethane-d2.
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Figure 10. 13C NMR spectrum of the polyethylene produced using Fe4/MMAO operating at 80 °C (entry 5, Table 2); recorded at 100 °C in 1,1,2,2-tetrachloroethane-d2.
Figure 10. 13C NMR spectrum of the polyethylene produced using Fe4/MMAO operating at 80 °C (entry 5, Table 2); recorded at 100 °C in 1,1,2,2-tetrachloroethane-d2.
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Figure 11. Bar chart showing the ratio of unsaturated to saturated chains for the polymer obtained as a function of run temperature using Fe4/MMAO as catalyst (entries 1–5, Table 2).
Figure 11. Bar chart showing the ratio of unsaturated to saturated chains for the polymer obtained as a function of run temperature using Fe4/MMAO as catalyst (entries 1–5, Table 2).
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Figure 12. Bar chart showing the ratio of unsaturated to saturated chains for the polymer obtained as a function of run temperature using Fe4/MAO as catalyst (entries 1–5, Table 3).
Figure 12. Bar chart showing the ratio of unsaturated to saturated chains for the polymer obtained as a function of run temperature using Fe4/MAO as catalyst (entries 1–5, Table 3).
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Table 1. Selected bond lengths and angles for Fe2 and Fe3.
Table 1. Selected bond lengths and angles for Fe2 and Fe3.
Fe2Fe3
Bond lengths (Å)
Fe(1)–N(2)2.142(5)2.076(3)
Fe(1)–N(1)2.241(5)2.228(2)
Fe(1)–N(3)2.240(5)2.169(3)
Fe(1)–Cl(1)2.2824(18)2.2537(10)
Fe(1)–Cl(2)2.3023(19)2.3177(9)
N(1)–C(2)1.277(8)1.208(15)
N(1)–C(21)1.441(7)1.443(4)
N(3)–C(13)1.286(9)1.281(15)
N(3)–C(33)1.436(8)1.447(4)
Bond angles (°)
Cl(1)–Fe(1)–Cl(2)107.94(9)116.77(4)
N(2)–Fe(1)–Cl(1)137.74(15)152.59(9)
N(2)–Fe(1)–Cl(2)114.30(15)90.63(8)
N(1)–Fe(1)–Cl(1)103.03(14)98.63(7)
N(1)–Fe(1)–Cl(2)98.74(15)102.38(7)
N(3)–Fe(1)–Cl(1)99.50(15)100.58(8)
N(3)–Fe(1)–Cl(2)99.99(16)99.99(8)
N(3)–Fe(1)–N(1)144.49(19)139.70(11)
N(2)–Fe(1)–N(1)72.52(18)73.13(9)
N(2)–Fe(1)–N(3)72.32(18)73.54(10)
Table 2. Ethylene polymerization screening using Fe1–Fe5 with MMAO as activator a.
Table 2. Ethylene polymerization screening using Fe1–Fe5 with MMAO as activator a.
EntryPrecat.Al:FeT (°C)t (min)Mass of PE (g)Activity bMwcMw/MncTm (°C) d
1Fe4250040305.1410.2851.614.2131.1
2Fe4250050308.6917.3835.610.7129.8
3Fe4250060309.5719.149.83.1130.0
4Fe4250070308.9117.824.81.5127.7
5Fe4250080303.667.323.71.5128.8
6Fe4150060302.575.1446.02.8132.4
7Fe4175060309.7519.5036.22.7133.1
8Fe42000603017.0534.1081.39.6131.8
9Fe42250603012.5025.0085.17.0132.8
10Fe420006058.1297.4413.73.5128.8
11Fe42000601511.2745.0823.03.9131.2
12Fe42000604518.0124.0190.69.1135.3
13Fe42000606018.2418.2494.39.2132.6
14 eFe4200060300.611.220.81.3120.2
15 fFe4200060308.9817.9679.07.4132.0
16Fe12000603012.8925.7826.46.4129.5
17Fe22000603014.6729.3470.06.9131.9
18Fe3200060305.3310.6651.68.1131.1
19Fe5200060303.827.6469.413.6130.1
a Conditions: MMAO as an activator, 1.0 μmol of the iron precatalyst, 100 mL of toluene, and 10 atm of ethylene; b Values in units of 106 g (PE) mol−1 (Fe) h−1; c Mw and Mn in units of kg mol−1, determined by GPC; d Determined by DSC; e 1 atm of ethylene; f 5 atm of ethylene.
Table 3. Ethylene polymerization screening using Fe1–Fe5 with MAO as activator a.
Table 3. Ethylene polymerization screening using Fe1–Fe5 with MAO as activator a.
EntryPrecat.Al:FeT (°C)t (min)Mass of PE (g)Activity bMwcMw/MncTm (°C) d
1Fe4250040306.0412.0895.518.5130.2
2Fe42500503010.0320.0672.411.7130.7
3Fe42500603015.2930.5865.08.8131.7
4Fe4250070309.8519.7018.43.0130.3
5Fe4250080305.0510.104.91.5132.7
6Fe41000603010.5421.08161.28.4132.1
7Fe41500603012.5225.04152.513.8132.3
8Fe42000603017.9635.92129.011.4132.3
9Fe43000603014.8029.6032.34.3130.7
10Fe420006057.0884.9616.83.8129.4
11Fe42000601511.0544.2029.76.1130.0
12Fe42000604518.1324.17142.115.4131.5
13Fe42000606018.6518.65168.016.6133.0
14 eFe4200060300.841.683.44.0124.8
15 fFe4200060307.0414.08130.713.0132.7
16Fe12000603014.1028.2048.98.8131.1
17Fe22000603010.1820.3659.28.5131.4
18Fe3200060306.5213.0435.27.0131.4
19Fe5200060308.7317.4650.28.8132.2
a Conditions: MAO as an activator, 1.0 μmol of the iron precatalyst, 100 mL of toluene, 10 atm of ethylene; b Values in units of 106 g (PE) mol−1 (Fe) h−1; c Mw and Mn in units of kg mol−1, determined by GPC; d Determined by DSC; e 1 atm of ethylene; f 5 atm of ethylene.
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Wang, Y.; Wang, Z.; Zhang, Q.; Ma, Y.; Solan, G.A.; Sun, Y.; Sun, W.-H. Non-Symmetrically Fused Bis(arylimino)pyridines with para-Phenyl Substitution: Exploring Their Use as N′,N,N″-Supports in Iron Ethylene Polymerization Catalysis. Catalysts 2024, 14, 213. https://doi.org/10.3390/catal14030213

AMA Style

Wang Y, Wang Z, Zhang Q, Ma Y, Solan GA, Sun Y, Sun W-H. Non-Symmetrically Fused Bis(arylimino)pyridines with para-Phenyl Substitution: Exploring Their Use as N′,N,N″-Supports in Iron Ethylene Polymerization Catalysis. Catalysts. 2024; 14(3):213. https://doi.org/10.3390/catal14030213

Chicago/Turabian Style

Wang, Yizhou, Zheng Wang, Qiuyue Zhang, Yanping Ma, Gregory A. Solan, Yang Sun, and Wen-Hua Sun. 2024. "Non-Symmetrically Fused Bis(arylimino)pyridines with para-Phenyl Substitution: Exploring Their Use as N′,N,N″-Supports in Iron Ethylene Polymerization Catalysis" Catalysts 14, no. 3: 213. https://doi.org/10.3390/catal14030213

APA Style

Wang, Y., Wang, Z., Zhang, Q., Ma, Y., Solan, G. A., Sun, Y., & Sun, W.-H. (2024). Non-Symmetrically Fused Bis(arylimino)pyridines with para-Phenyl Substitution: Exploring Their Use as N′,N,N″-Supports in Iron Ethylene Polymerization Catalysis. Catalysts, 14(3), 213. https://doi.org/10.3390/catal14030213

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