Yuting Zhengab,
Shu Jiangab,
Ming Liub,
Zhixin Yu*a,
Yanping Mabc,
Gregory A. Solan*bc,
Wenjuan Zhangbd,
Tongling Liangb and
Wen-Hua Sun*b
aSchool of Pharmaceutical Sciences, Changchun University of Chinese Medicine, Changchun 130117, China. E-mail: yuzx01@ccucm.edu.cn
bKey Laboratory of Engineering Plastics, Beijing National Laboratory for Molecular Sciences, Institute of Chemistry, Chinese Academy of Sciences, Beijing 100190, China. E-mail: gas8@leicester.ac.uk; whsun@iccas.ac.cn
cDepartment of Chemistry, University of Leicester, University Road, Leicester LE1 7RH, UK
dBeijing Key Laboratory of Clothing Materials R&D and Assessment, Beijing Engineering Research Center of Textile Nanofiber, School of Materials Science and Engineering, Beijing Institute of Fashion Technology, Beijing 100029, China
First published on 1st September 2022
The following family of N,N-diaryl-2,3-dimethyl-1,4-diazabutadienes, ArNC(Me)C(Me)NAr (Ar = 2,6-Me2-4-{CH(4-FC6H4)2}C6H2 L1, 2-Me-6-Et-4-{CH(4-FC6H4)2}C6H2 L2, 2,4-{CH(4-FC6H4)2}2-6-MeC6H2 L3, 2,4-{CH(4-FC6H4)2}2-6-EtC6H2 L4, 2,4-{CH(4-FC6H4)2}2-6-iPrC6H2 L5), each incorporating para-substituted 4,4-difluorobenzhydryl groups but differing in the ortho-pairing, have been synthesized and used as precursors to their respective nickel(II) bromide complexes, Ni1–Ni5. Compound characterization has been achieved through a combination of FT-IR, multinuclear NMR spectroscopy (1H, 13C, 19F) and elemental analysis. In addition, L1, Ni1 and Ni5 have been structurally characterized with Ni1 and Ni5 revealing similarly distorted tetrahedral geometries about nickel but with distinct differences in the steric protection offered by the ortho-substituents. All nickel complexes, under suitable activation, showed high activity for ethylene polymerization with a predilection towards forming branched high molecular weight polyethylene with narrow dispersity. Notably the most sterically bulky Ni5, under activation with either EtAlCl2, Et2AlCl or EASC, was exceptionally active (0.9–1.0 × 107 g of PE per (mol of Ni) per h) at an operating temperature of 40 °C. Furthermore, the polyethylene generated displayed molecular weights close to one million g mol−1 (Mw range: 829–922 kg mol−1) with high branching densities (86–102/1000 carbons) and a selectivity for short chain branches (% Me = 94.3% (EtAlCl2), 87.2% (Et2AlCl), 87.7% (EASC)). Further analysis of the mechanical properties of the polymers produced at 40 °C and 50 °C using Ni5 highlighted the key role played by crystallinity (Xc) and molecular weight (Mw) on tensile strength (σb) and elongation at break (εb). In addition, stress–strain recovery tests reveal these high molecular weight polymers to exhibit characteristics of thermoplastic elastomers (TPEs).
With particular regard to α-diimino-nickel catalysts, great advances have been made over the last few years with regard to improvements in thermal stability and catalytic activity of their active species. These developments have largely been concerned with modifying the ligand backbone and changing the substituents on the imino N-aryl groups.3c In terms of our contribution to the area, we have examined in some depth the scope of non-symmetric 1,2-bis(imino)acenaphthene-nickel(II) halide complexes (A, Chart 1), where one N-aryl group is appended with sterically bulky benzhydryl (CHPh2) or its fluorinated derivatives, e.g., Ar1 = 2,6-dibenzhydryl-4-R,8 2,6-bis(difluorobenzhydryl)-4-R,9 2,4-dibenzhydryl-6-R10 and 2,4-bis(difluorobenzhydryl)-6-R11 (R = alkyl, halide and aryl). As a result, certain conclusions can be drawn from these investigations, including the increased thermostability of these catalysts and the enhanced catalytic activity, particularly for the 4,4-difluorobenzhydryl-substituted systems; polyethylenes generated can vary from low molecular weight to narrowly dispersed high molecular weight. From our viewpoint, these fundamental studies can help accelerate the synthesis of an industrially relevant α-diimine catalyst that can achieve precise regulation of the polymer.
Chart 1 α-Diimino-nickel(II) halide complexes based on unsymmetrical 1,2-bis(arylimino)acenaphthenes (A) and 2,3-dimethyl-1,4-diazabutadienes (B) along with target precatalyst, C. |
By the same token, N,N′-diaryl-2,3-dimethyl-1,4-diazabutadiene-nickel complexes (B, Chart 1) incorporating 2,6-bis(difluorobenzhydryl) groups on one side of the ligand frame, have shown encouraging results by producing highly branched polyethylene with high molecular weight that can sometimes display bimodal distributions.12 As with the A-type precatalysts, the presence of the fluoro-substituents has been demonstrated to have a beneficial effect on both catalytic activity as well as on the thermal stability.
As part of our current program, we are aiming to expand the types of nickel catalyst by harnessing the positive influence of the 4,4-difluorobenzhydryl groups on catalytic activity and other properties.9,11 In particular, we report herein a new series of symmetrical N,N-diaryl-2,3-dimethyl-1,4-diazabutadiene-nickel precatalysts (C, Chart 1), that all contain one para-4,4-difluorobenzhydryl substituent per N-aryl group but differ in the pairings for the ortho-substituents ((Me/Me, Me/Et, Me/(p-FPh)2CH), Et/(p-FPh)2CH, iPr/(p-FPh)2CH). We considered that this progressive increase in the steric properties of the ortho-substitution pattern would not only impact on catalytic activity and thermostability, but also on the polymer molecular weight and the degree and composition of branching. The control of the latter being central to the development of elastomeric polyethylene with high molecular weight.13 Consequently, a thorough ethylene polymerization study is described to explore these changes, and also probe the influence of co-catalyst type, run temperature and ethylene pressure. All ligands and complexes are new and so full details for ligand synthesis and complexation are reported. Furthermore, the potential for isomeric species in the ligand, precatalyst and catalyst offers additional points of interest.
Scheme 1 Synthetic route to the N,N-diaryl-2,3-dimethyl-1,4-diazabutadienes (L1–L5) and their nickel(II) bromide complexes (Ni1–Ni5). |
Several isomers are possible for L1–L5 on the basis of Z,E-isomerism about the CN bonds, s-cis/s-trans isomerism and anti/syn isomerism as a result of hindered rotation of the N-aryl groups (Scheme 2).5g,h,j,6c,15 Given that L2 (R1 = Me, R2 = Et) shows peaks for one compound in its 1H NMR spectrum (see Fig. S2†), it would suggest that E,E/Z,E and s-cis/s-trans interconversions for both L2-anti and L2-syn are fast on the laboratory timescale at room temperature. By contrast for L3–L5, two isomers were seen in their 1H NMR spectra in ratios of approximately 5:1 which we have attributed to the presence of anti and syn isomers, respectively (see Fig. S3–S5†). In these cases the steric properties of the sterically bulky ortho-CH(p-FPh)2 groups are considered to impede N-aryl rotation resulting in an enriched anti conformer. Similar observations are seen in the fluorine-free comparators of L3–L5.5k The 1H NMR spectra of the complexes were all broad and paramagnetically shifted (S = 1) (see Fig. S21–S25†). For example, the 1H NMR spectrum of Ni4 displayed two broad signals around δH 24 and δH 28 ppm for its ortho-ethyl groups due to its steric hindrance16 (see Fig. S24†). By comparison for Ni2, at least three broad resonances are observed in the δH 24–28 ppm region Ni2 (see Fig. S22†), which would suggest the presence of both Ni2-anti and Ni2-syn forms. Similar phenomena were seen in the 1H NMR spectra of Ni3–Ni5 (see Fig. S14 and S25†), which were likely due to the characteristic temperature dependence and relaxation effects of paramagnetic complexes.16,17
Scheme 2 Some possible isomers for L1–L5 based on E/Z isomerism, s-cis/s-trans isomerism and anti/syn isomerism; where ϕ = CH(p-FPh)2. |
In the 19F NMR spectrum of L1 a single broad peak at δ −116.85 ppm was seen on account of the equivalent para-4,4-difluorobenzhydryl groups, which is slightly downfield shifted on coordination to nickel (see Fig. S26a† for spectra of L1 and Ni1). By contrast in L3, the 19F NMR spectrum showed three distinct fluoride resonances, two closely located signals at δ −116.69 and −116.80 ppm, and another more downfield at δ −115.87 ppm. By comparison with L1, the more intense resonance at δ −116.69 can be assigned to the freely rotating para-4,4-difluorobenzhydryl groups, while the other two resonances to inequivalent CH(4-FC6H4)a(4-FC6H4)b groups on account of restricted rotation due to the proximity of the imine-methyl group,18 further evidence for this restricted rotation can be detected in the 13C NMR spectra (see Fig. S5–S10†). Similarly, complex Ni3 display three fluoride resonances in an approximate 1:2:1 ratio (Fig. 1b and S28†), with the signals at δ −114.44 and δ −116.38 ppm assignable to the ortho-CH(4-FC6H4)a(4-FC6H4)b groups, while the third resonance centered at δ −115.33 ppm to the para-4,4-difluorobenzhydryl substituent. Closer inspection of this latter signal, however, reveals it to comprise two closely located resonances, which would suggest that some restricted Cpara-aryl rotation is also possible in the complex. Notably, in Ni4 these signals for the para-CH(4-FC6H4)a(4-FC6H4)b groups become more distinct (Fig. S29†).
Fig. 1 ORTEP drawing of L3 (molecule A). Thermal ellipsoids are shown at the 30% probability level while the hydrogen atoms have been omitted for clarity. |
Single crystals of L3, Ni2 and Ni5 of appropriate quality for the X-ray determination were obtained by layering dichloromethane solutions of each compound with diethyl ether. The structures of L3, Ni1 and Ni5 are depicted in Fig. 2–4, while selected bond lengths and angles are collected in Table 1. For Ni5 two independent molecules (A and B) were present in the asymmetric unit while in L3 there were three (A, B and C). As the molecules showed only minimal differences, only molecule A for each structure will be discussed in any detail. For the two nickel complexes, Ni1 and Ni5, the structures are similar and based on a four coordinate nickel center bound by a bidentate N,N-diaryl-2,3-dimethyl-1,4-diazabutadiene ligand (aryl = 2,6-dimethyl-4-bis(4-fluorophenyl)methylphenyl Ni1 and 2,4-di{bis(4-fluorophenyl)methyl}-6-isopropylphenyl Ni5) and two monodentate bromide ligands. In terms of geometry, this can be described as distorted tetrahedral which is in part enforced by the N–Ni–N bite angle of the N,N-chelating ligand [81.2(3)° Ni1, 81.7(3)° Ni5]. Notably, there is some variation in the Br1–Ni1–Br2 angles between the two structures (123.15(9)° Ni1, 116.69(9)° Ni5), which may relate to the differences in substitution pattern on the N-aryl groups. The Ni–N bond lengths in both structures are comparable [Ni(1)–N(1) 2.024(8) Å (Ni1), 2.009(9) Å (Ni5); Ni(1)–N(2) 2.006(9) Å (Ni1), 2.014(8) Å (Ni5)], as are the Ni–Br lengths [Ni(1)–Br(1) 2.338(2) Å (Ni1), 2.336(2) Å (Ni5); Ni(1)–Br(2) 2.317(2) Å (Ni1), 2.326(2) Å (Ni5)] and indeed consistent with that found in previous reports.8a,19–22 The planes of the N-aryl groups are almost perpendicular to the coordination plane C3–C4–N1–Ni–N2, as evidenced by the dihedral angles for Ni1 (83.25°, 88.55°) and Ni5 (81.20°, 78.94°). By comparison, the structure of the free ligand, L3, shows a E,E-s-trans configuration with the bulky ortho-substituents on each N-aryl ring adopting an anti conformer; such a transoid disposition of the imine nitrogens in 1,4-diazabutadienes is commonplace.15 The C–Nimine bond lengths (N1–C3 1.276(3) Å, N2–C4 1.270(3) Å) are nonetheless similar to that seen in complexes Ni1 (N1–C3 1.288(13) Å, N2–C4 1.323(12) Å) and Ni5 (N1–C3 1.291(12) Å, N2–C4 1.286(12) Å). The 4,4-difluorobenzhydryl substituents in each of the three structures show no unusual features.
Fig. 2 ORTEP drawing of Ni1. Thermal ellipsoids are shown at the 30% probability level while the hydrogen atoms have been omitted for clarity. |
Fig. 3 ORTEP drawing of Ni5 (molecule A). Thermal ellipsoids are shown at the 30% probability level while the hydrogen atoms have been omitted for clarity. |
L3 (molecule A) | Ni1 | Ni5 (molecule A) | |
---|---|---|---|
Br(1)–Ni(1) | — | 2.336(2) | 2.338(2) |
Br(2)–Ni(1) | — | 2.326(2) | 2.317(2) |
Ni(1)–N(1) | — | 2.009(9) | 2.007(8) |
Ni(1)–N(2) | — | 2.014(8) | 2.019(7) |
N(1)–C(3) | 1.276(3) | 1.288(13) | 1.291(12) |
N(2)–C(4) | 1.270(3) | 1.323(12) | 1.286(12) |
N(1)–C(5) | 1.413(2) | 1.433(12) | 1.413(13) |
C(4)–C(3) | 1.502(3) | 1.493(14) | 1.498(14) |
C–F (range) | 1.352(3)-1.364(2) | 1.349(13)-1.376(13) | 1.359(14)-1.381(15) |
Br(2)–Ni(1)–Br(1) | — | 123.15(9) | 116.69(9) |
N(2)–Ni(1)–Br(1) | — | 116.4(2) | 116.4(2) |
N(2)–Ni(1)–Br(2) | — | 109.2(2) | 109.2(2) |
N(1)–Ni(1)–Br(1) | — | 100.4(3) | 100.4(3) |
N(1)–Ni(1)–Br(2) | — | 118.6(2) | 118.6(2) |
N(1)–Ni(1)–N(2) | — | 81.7(3) | 81.7(3) |
C(4)–C(3)–N(1) | 115.97(19) | 117.0(8) | 116.6(8) |
C(3)–C(4)–N(2) | 115.45(10) | 114.6(8) | 115.0(8) |
Entry | Co-cat. | Al:Ni | Activityb | Mwc | Mw/Mnc | Tmd (°C) |
---|---|---|---|---|---|---|
a General conditions: 2 μmol of Ni2, 30 °C, 30 min, 10 atm ethylene, 100 mL toluene.b ×106 g of PE per (mol of Ni) per h.c Determined by GPC, Mw in units of ×105 g mol−1.d Determined by DSC. | ||||||
1 | MAO | 2000 | 6.84 | 2.25 | 2.27 | 105.5 |
2 | MMAO | 2000 | 4.11 | 2.53 | 2.62 | 112.4 |
3 | EtAlCl2 | 400 | 5.21 | 2.53 | 2.55 | 104.4 |
4 | Et2AlCl | 400 | 4.81 | 1.91 | 2.72 | 106.3 |
5 | EASC | 400 | 4.08 | 2.34 | 3.12 | 106.8 |
Entry | Precat. | T (°C) | t (min) | Al:Ni | Act.b | Mwc | Mw/Mnc | Tmd (°C) |
---|---|---|---|---|---|---|---|---|
a General conditions: 2 μmol of nickel precatalyst, 30 °C, 30 min, 10 atm ethylene, 100 mL toluene.b ×106 g of PE per (mol of Ni) per h.c Determined by GPC, Mw in units of ×105 g mol−1.d Determined by DSC.e 5 atm of ethylene.f 1 atm of ethylene. | ||||||||
1 | Ni2 | 30 | 30 | 1000 | 1.12 | 5.39 | 2.59 | 127.6 |
2 | Ni2 | 30 | 30 | 1500 | 7.17 | 3.13 | 2.58 | 107.5 |
3 | Ni2 | 30 | 30 | 2000 | 6.84 | 2.25 | 2.27 | 105.2 |
4 | Ni2 | 30 | 30 | 2500 | 6.12 | 2.14 | 2.44 | 116.0 |
5 | Ni2 | 30 | 30 | 3000 | 5.76 | 1.86 | 2.68 | 111.3 |
6 | Ni2 | 20 | 30 | 1500 | 1.05 | 6.14 | 2.34 | 129.6 |
7 | Ni2 | 40 | 30 | 1500 | 3.56 | 2.25 | 2.77 | 121.5 |
8 | Ni2 | 50 | 30 | 1500 | 2.48 | 1.80 | 2.20 | 118.7 |
9 | Ni2 | 60 | 30 | 1500 | 1.02 | 1.00 | 3.06 | 93.4 |
10 | Ni2 | 30 | 5 | 1500 | 15.60 | 2.31 | 2.73 | 116.5 |
11 | Ni2 | 30 | 15 | 1500 | 11.84 | 3.12 | 2.14 | 113.3 |
12 | Ni2 | 30 | 45 | 1500 | 5.11 | 3.18 | 2.00 | 124.9 |
13 | Ni2 | 30 | 60 | 1500 | 3.94 | 4.05 | 2.92 | 126.4 |
14e | Ni2 | 30 | 30 | 1500 | 2.77 | 2.42 | 2.43 | 121.1 |
15f | Ni2 | 30 | 30 | 1500 | 0.08 | 0.71 | 5.51 | 65.4 |
16 | Ni1 | 30 | 30 | 1500 | 6.01 | 9.11 | 2.88 | 111.3 |
17 | Ni3 | 30 | 30 | 1500 | 3.93 | 9.42 | 2.18 | 116.6 |
18 | Ni4 | 30 | 30 | 1500 | 1.54 | 3.63 | 2.75 | 116.9 |
19 | Ni5 | 30 | 30 | 1500 | 1.13 | 10.48 | 2.37 | 95.5 |
20 | Ni5 | 40 | 30 | 1500 | 3.17 | 8.67 | 2.49 | 68.1 |
21 | Ni5 | 50 | 30 | 1500 | 1.01 | 7.44 | 2.65 | 63.1 |
With the temperature maintained at 30 °C, the Al:Ni molar ratio using Ni2/MAO was subject to a stepwise increase from 1000:1 to 3000:1 (entries 1–5, Table 3). Initially the activity was seen to rise reaching a highpoint of 7.17 × 106 g of PE per (mol of Ni) per h with the ratio at 1500:1, then as the ratio was increased further the activity progressively decreased. As a further point, the activity was seen to increase sharply when the Al:Ni molar ratio was adjusted from 1000:1 to 1500:1, which suggests there is a critical amount of MAO required before good activity can be achieved. As has been previously observed, the amount of MAO employed can influence the molecular weight of the polymer.9a–c,11,12,19,22–24 Similarly in this case, an increase in the Al:Ni molar ratio led to a decrease in the value of Mw from 539 kg mol−1 at 1000:1 to 186 kg mol−1 at 3000:1 (Fig. S32†). It would seem likely that termination of the polymerization involving chain transfer to aluminum is to some extent operational with larger ratios of MAO.8b,f,9d,11 Some support for this is provided by the absence of detectable downfield vinylic peaks in the δ 110 − 140 region (Fig. S40†) of the 13C NMR spectrum of the polymer (see later), although the high molecular weight of this polymer may also explain this absence.
With the Al:Ni molar ratio retained at 1500:1, the polymerization runs using Ni2/MAO were performed at five distinct temperatures ranging from 20 °C to 60 °C. Examination of the data revealed that at 30 °C, the activity of 7.17 × 106 g of PE per (mol of Ni) per h remained the highest (entry 2, Table 3). It was apparent that on raising the temperature beyond 30 °C, the rate of chain transfer increased while the active species showed some evidence of deactivation.25 Meanwhile, the influence of temperature on the molecular weight of the polymer was similar than that seen with a change in the Al:Ni molar ratio. In particular, on raising the temperature of the run, the molecular weight of the polymer decreased from 614 kg mol−1 at 20 °C to 100 kg mol−1 at 60 °C (Fig. S33†); a finding that can be attributed to thermally induced chain transfer.8b,f,9d,10a,11
With the temperature and the amount of MAO retained at 30 °C and 1500 equivalents, respectively, the impact of run time on the performance of Ni2/MAO was explored. By employing set times between 5 minutes and 60 minutes (entries 2, 10–13, Table 3), it was noted that the peak activity was observed after 5 minutes with levels reaching up to 15.6 × 106 g of PE per (mol of Ni) per h. Such a highpoint in activity early in the run would imply rapid formation of the active species followed by gradual catalyst deactivation.6c Nonetheless, even after one hour, the activity still remained at an appreciable level [3.94 × 106 g of PE per (mol of Ni) per h] highlighting the significant lifetime displayed by this catalyst. Further studies showed that the response of Ni2/MAO to variations in ethylene pressure were consistent with previous studies,19 with a lowering in the pressure leading to a reduction in the activity (entries 14 and 15, Table 3). Concomitantly, the molecular weight of the polymer decreased, and the dispersity broadened. It would seem plausible that a reduced ethylene pressure would result in mass transport limitations of the ethylene monomer leading to an increase in the rate of chain transfer to aluminum, thereby decreasing the molecular weight of the polymer.6c,8g
With an effective set of reaction conditions now established for Ni2/MAO, the remaining precatalysts, Ni1, Ni3–Ni5, were then evaluated similarly with the aim to explore the influence of structural changes to the ligand frame on catalytic performance (entries 16–19, Table 3). All catalysts displayed good activity (1.13–7.17 × 106 g of PE per (mol of Ni) per h) generating polymers that showed narrow dispersities (Mw/Mn range: 2.18–2.88). Overall, the order of activity was as follows: Ni2 [2-Me-6-Et-4-(4,4-difluorobenzhydryl)] > Ni1 [2,6-Me2-4-(4,4-difluorobenzhydryl)] > Ni3 [2,4-di(4,4-difluoro-benzhydryl)-6-Me] > Ni4 [2,4-di(4,4-difluorobenzhydryl)-6-Et] > Ni5 [2,4-di(4,4-difluorobenzhydryl)-6-iPr].
Several points emerge from inspection of this order. Firstly, the precatalysts incorporating the less sterically bulky ortho-substituents, Ni1 (Me/Me) and Ni2 (Me/Et) proved the most active, which is consistent with previous observations.21 Of these two systems, Ni2 showed the highest productivity [7.17 × 106 g of PE per (mol of Ni)], which may originate from favorable electronic or steric factors imparted by the possible syn/anti conformers; this is, however, far from clear.5g,6,7 Secondly, it is apparent that the incorporation of one sterically bulky ortho-(4,4-difluorobenzhydryl) group per N-aryl unit depressed activity at this temperature. It is possible that the anti/syn mixture seen in L3–L5, may not in this case be beneficial to the polymerization if reproduced in Ni3–Ni5. Nonetheless, for the three catalysts based on this substitution pattern (Ni3, Ni4 and Ni5), the steric properties of the second ortho-substituent (Me, Et, iPr) proved influential with 6-methyl Ni3 more active than 6-isopropyl Ni5.
By contrast, in terms of polymer molecular weight the order follows: Ni5 [2,4-di(4,4-difluorobenzhydryl)-6-iPr] > Ni3 [2,4-di(4,4-difluorobenzhydryl)-6-Me] > Ni1 [2,6-Me2-4-(4,4-difluorobenzhydryl)] > Ni4 [2,4-di(4,4-difluorobenzhydryl)-6-Et] > Ni2 [2-Me-6-Et-4-(4,4-difluorobenzhydryl)]. Interestingly, for ortho-ethyl substituted Ni2 and Ni4, the molecular weight of the resulting polymers was notably lower than that seen with the other catalysts (Mw range: 313–363 kg mol−1). However, it remains unclear as to how this structural variation makes it more amenable to chain transfer.6c,8g On the other hand, the molecular weight of the polymer produced using the most sterically bulky Ni5 was more than a million g mol−1 (i.e., 1048 kg mol−1, entry 19, Table 3); see Fig. S30† for a pictorial representation of the molecular weight variations. Notably, when compared with their non-fluorinated benzhydryl comparators,21,26 these MAO-activated para-4,4-difluorobenzhydryl-substituted nickel complexes exhibited higher activities (see later). Such a finding is consistent with the electron-withdrawing fluoride substituents enhancing the Lewis acidity of the active metal species leading to more effective monomer coordination and insertion.27–29
To probe the response of ortho-(4,4-difluorobenzhydryl)-substituted Ni5 to run temperature, we also investigated Ni5/MAO at temperatures in excess of 30 °C. Significantly, this catalyst almost trebled its level of activity when the temperature was raised to 40 °C (3.17 × 106 g of PE per (mol of Ni) per h), a finding that underlines the capacity of the bulky ortho-CH(4-FC6H4)2 group to improve the thermal stability of the catalyst. A plausible explanation can be attributed to the increased spatial volume present at the ortho-position leading to an enhanced shielding effect on the axial positions in the active nickel catalyst, thus inhibiting the chain transfer.1a,4a
Entry | Precat. | T (°C) | t (min) | Al:Ni | Act.b | Mwc | Mw/Mnc | Tmd (°C) |
---|---|---|---|---|---|---|---|---|
a General conditions: 2 μmol of nickel precatalyst, 30 °C, 30 min, 10 atm ethylene, 100 mL toluene.b ×106 g of PE per (mol of Ni) per h.c Determined by GPC, Mw in units of ×105 g mol−1.d Determined by DSC.e 5 atm of ethylene.f 1 atm of ethylene.g Ni5 in combination with Et2AlCl.h Ni5 in combination with EASC. | ||||||||
1 | Ni2 | 30 | 30 | 300 | 3.28 | 2.34 | 2.87 | 107.7 |
2 | Ni2 | 30 | 30 | 400 | 5.21 | 2.53 | 2.55 | 104.4 |
3 | Ni2 | 30 | 30 | 500 | 5.83 | 2.48 | 2.59 | 106.3 |
4 | Ni2 | 30 | 30 | 600 | 6.48 | 2.05 | 2.79 | 99.0 |
5 | Ni2 | 30 | 30 | 700 | 4.84 | 2.63 | 2.05 | 110.1 |
6 | Ni2 | 30 | 30 | 800 | 4.24 | 2.48 | 2.31 | 112.7 |
7 | Ni2 | 20 | 30 | 600 | 5.30 | 3.64 | 2.73 | 116.5 |
8 | Ni2 | 40 | 30 | 600 | 5.82 | 1.18 | 1.96 | 87.9 |
9 | Ni2 | 50 | 30 | 600 | 4.88 | 1.03 | 2.36 | 86.5 |
10 | Ni2 | 60 | 30 | 600 | 2.39 | 0.69 | 2.76 | 65.0 |
11 | Ni2 | 30 | 5 | 600 | 17.52 | 1.49 | 2.76 | 108.3 |
12 | Ni2 | 30 | 15 | 600 | 7.40 | 1.87 | 2.46 | 112.7 |
13 | Ni2 | 30 | 45 | 600 | 4.74 | 2.27 | 2.72 | 108.7 |
14 | Ni2 | 30 | 60 | 600 | 3.73 | 2.40 | 2.56 | 109.5 |
15e | Ni2 | 30 | 30 | 600 | 4.93 | 1.60 | 2.43 | 106.7 |
16f | Ni2 | 30 | 30 | 600 | 0.35 | 0.68 | 1.91 | 47.8 |
17 | Ni1 | 30 | 30 | 600 | 6.14 | 13.08 | 2.17 | 109.9 |
18 | Ni3 | 30 | 30 | 600 | 7.43 | 8.19 | 2.84 | 109.0 |
19 | Ni4 | 30 | 30 | 600 | 4.95 | 1.28 | 2.90 | 114.0 |
20 | Ni5 | 30 | 30 | 600 | 4.81 | 15.19 | 2.30 | 93.3 |
21 | Ni5 | 40 | 30 | 600 | 9.20 | 9.22 | 2.45 | 69.6 |
22 | Ni5 | 50 | 30 | 600 | 4.43 | 8.88 | 2.25 | 50.1 |
23g | Ni5 | 40 | 30 | 600 | 8.97 | 8.36 | 2.68 | 77.3 |
24h | Ni5 | 40 | 30 | 600 | 10.03 | 8.29 | 3.12 | 73.8 |
As with the Ni2/MAO study, Ni2/EtAlCl2 was first investigated at 30 °C with the Al:Ni molar ratio in this case adjusted from 300:1 to 800:1 (entries 1–6, Table 4). The results revealed that the peak activity of 6.48 × 106 g of PE per (mol of Ni) per h was achieved at 600:1 which compares with 7.17 × 106 g of PE per (mol of Ni) per h for Ni2/MAO. However, and unlike that seen for Ni2/MAO, the molecular weight of the polyethylene can be more precisely controlled with values typically around 200 kg mol−1 (Mw range: 205–263 kg mol−1), with significantly less influence caused by changing the amount of alkylaluminum. This finding would also suggest that the larger amounts of co-catalyst required in the MAO runs to allow effective precatalyst activation, also facilitated more effective chain transfer to MAO.8b,f,9d,11
As for the effect of run temperature, the activity of Ni2/EtAlCl2 and the molecular weight of the resulting polymer showed similar variations to that seen with Ni2/MAO (entries 4, 7–10, Table 4). Indeed, Ni2/EtAlCl2 also reached its maximum activity at 30 °C (6.48 × 106 g of PE per (mol of Ni) per h), but the increase in level from that noted at 20 °C (5.30 × 106 g of PE per (mol of Ni) per h) was less pronounced. Evidently, lower temperature can hinder the activation of Ni2 with MAO. Furthermore, Ni2/EtAlCl2 at 60 °C still maintained an appreciable level of activity (2.39 × 106 g of PE per (mol of Ni) per h) which by comparison is more than double that seen for Ni2/MAO (1.02 × 106 g of PE per (mol of Ni) per h) at the same temperature.
Likewise, the response to run time for Ni2/EtAlCl2 was similar to that found for Ni2/MAO with the former attaining its maximum activity after 5 minutes [17.52 × 106 g of PE per (mol of Ni) per h] and thereafter decreasing to 3.73 × 106 g of PE per (mol of Ni) per h at 60 minutes with the onset of catalyst deactivation. Nonetheless, the molecular weight gradually increased over time implying the presence of sufficient active species to sustain chain propagation (entries 4, 11–14, Table 4). On reducing the ethylene pressure of the run to 5 atm and then 1 atm saw the activity of Ni2/EtAlCl2 drop and the resulting molecular weight of the polymer fall; related findings has been reported in previous literature.9a,23b
As a common feature of the polymers generated during the optimization process for Ni2/EtAlCl2 was their narrow dispersity (Mw/Mn range: 1.91–2.87). Indeed, a similar observation was made with Ni2/MAO, which highlights the single-site nature of these catalysts and in turn the good control imparted on propagation. On the other hand, and as a notable difference, the molecular weight of the polymers produced by Ni2/MAO (Mw range: 100–614 kg mol−1) was in general higher when compared to that seen for Ni2/EtAlCl2 (Mw range: 69–364 kg mol−1) (vide infra).
Subsequently, we subjected Ni1, Ni3, Ni4 and Ni5, to the optimized conditions established for Ni2/EtAlCl2 (Al:Ni molar ratio = 600:1, T = 30 °C, run time = 30 min). All five precatalysts including Ni2 showed good activity spanning the range, 4.81–7.43 × 106 g of PE per (mol of Ni) per h (cf. 1.13–7.17 × 106 g of PE per (mol of Ni) per h for MAO). With respect to the relative performance, this order was: Ni3 [2,4-di(4,4-difluorobenzhydryl)-6-Me] > Ni2 [2-Me-6-Et-4-(4,4-difluorobenzhydryl)] > Ni1 [2,6-Me2-4-(4,4-difluorobenzhydryl)] > Ni4 [2,4-di(4,4-difluorobenzhydryl)-6-Et] > Ni5 [2,4-di(4,4-difluorobenzhydryl)-6-iPr]. Scrutiny of this downward trend highlights one key difference to that seen with MAO:Ni3, incorporating a sterically bulky ortho-substituent, is now the most active system of the series (7.43 × 106 g of PE per (mol of Ni) per h, entry 18, Table 4), rather than in third place as was seen with MAO. The main reason behind this observation remains unclear but it may be derive from the different binding capacities between the active nickel center and aluminum-based anion in the active species.30,31
In terms of the molecular weight of the polymers generated, these fell in a wider range than with MAO [Mw range: 128–1519 kg mol−1 (EtAlCl2) vs. 313–1048 kg mol−1 (MAO)] with the highest molecular weight material significantly greater with EtAlCl2. Pertaining to the precatalyst, the value of Mw falls in the order: Ni5 [2,4-di(4,4-difluorobenzhydryl)-6-iPr] > Ni1 [2,6-Me2-4-(4,4-difluorobenzhydryl)] > Ni3 [2,4-di(4,4-difluorobenzhydryl)-6-Me] > Ni2 [2-Me-6-Et-4-(4,4-difluorobenzhydryl)] ∼ Ni4 [2,4-di(4,4-difluorobenzhydryl)-6-Et]. In the main, this order resembles that seen with MAO with the most sterically bulky precatalyst Ni5 forming the highest molecular weight polymer, while ortho-ethyl containing Ni2 and Ni4, the lowest. Indeed, Ni5/EtAlCl2 is amenable to forming ultra-high molecular weight polyethylene (UHMWPE) with the run temperature at 30 °C; see Fig. S34† for a depiction of these trends. As with the MAO study, the reason why the ortho-ethyl-containing precatalysts (Ni2 and Ni4) have a tendency to form lower molecular weight polymer remains unclear; we nevertheless consider this a valuable feature for catalyst design.
As with Ni5/MAO, we also explored the performance of Ni5/EtAlCl2 at run temperatures of greater than 30 °C. Significantly, at 40 °C a dramatic increase in activity was observed with Ni5/EtAlCl2 reaching a value of 9.20 × 106 g of PE per (mol of Ni) per h that equates to a 90% improvement in activity; even at 50 °C the level only dropped to 4.43 × 106 g of PE per (mol of Ni) per h (cf. MAO for 3.17 × 106 g of PE per (mol of Ni) per h at 40 °C and 1.01 × 106 g of PE per (mol of Ni) per h at 50 °C). Evidently, both Ni5/MAO and Ni5/EtAlCl2 show heightened performance characteristics at higher run temperature which is particular true for EtAlCl2, which evidently reflects the enhanced thermal stability of the active species formed with this co-catalyst. Though numerous publications of the use of 2,3-dimethyl-1,4-diazabutadiene-nickel precatalysts in ethylene polymerization have been reported,1g,3b,4,5f,12,13,19–21,26 relatively few have been concerned with the generation of polyethylene elastomers at higher run temperature. However in those cases, the elastomeric materials tend to be of too low a molecular weight. It is noteworthy that with the current modification to the N,N-ligand frame, the catalyst, Ni5/EtAlCl2, displays not only enhanced thermal stability, but also produces polyethylene elastomers displaying amongst the highest molecular weights (9.22 × 105 g mol−1 at 40 °C and 8.88 × 105 g mol−1 at 50 °C).
In order to further probe the outstanding performance characteristics displayed by Ni5 at higher temperature, we extended the investigation to include two other aluminum-alkyl co-catalysts namely EASC and Et2AlCl (entries 23 and 24, Table 4). While Ni5/Et2AlCl showed similar performance to Ni5/EtAlCl2 (entry 21 vs. 23, Table 4), the activity of Ni5/EASC reached an exceptional level of 1.0 × 107 g of PE per (mol of Ni) per h at 40 °C (entry 24, Table 4), which is to the knowledge of the authors among one the highest reported for α-diimine-nickel complexes operating at this temperature. Furthermore, the molecular weight of the polyethylene obtained using both Ni5/Et2AlCl and Ni5/EASC remained exceptionally high. To illustrate these results, Fig. 4 collects together catalytic activity and polymer molecular weight data for Ni5/Et2AlCl alongside that produced using selected examples of A (Chart 1) as well as fluorine-free analogues of the current precatalysts C;8b–g,9b,11,21 all catalytic runs were performed under comparable conditions and co-catalyst. As a further point that can be gleaned from inspection of this figure, it is apparent that the introduction of electron-withdrawing fluoro-substituents in Ni5 enhances catalytic activity, findings that are consistent with previously reported experimental observations9,11 and calculations.27–29
PE sample | Branches/1000Cs | Branching composition (%) | ||||||
---|---|---|---|---|---|---|---|---|
Me | Et | Pr | Bu | Amyl | Me (1,4-paired) | Me (1,6-paired) | ||
a Data obtained using 13C NMR spectroscopy.b Analysis performed using approaches described in ref. 32. | ||||||||
PE-M30Ni2 | 50 | 70.9 | 3.22 | 3.04 | 6.30 | 2.79 | 4.39 | 4.76 |
PE-EtAlCl240Ni5 | 86 | 81.6 | 1.17 | 0.07 | 2.50 | 0.68 | 6.58 | 5.63 |
PE-Et2AlCl40Ni5 | 86 | 75.9 | 1.90 | 1.43 | 2.67 | 1.51 | 5.76 | 5.51 |
PE-EASC40Ni5 | 102 | 72.2 | 3.09 | 1.39 | 2.64 | 1.52 | 7.92 | 7.60 |
On examination of the results, it is apparent that all four polyethylene samples contain a significant amount of branching that would be expected on the basis of a chain walking mechanism.33 Notably, the polymers obtained using Ni5/EtAlCl2, Ni5/Et2AlCl and Ni5/EASC displayed a higher degree of branching than that seen with Ni2/MAO and also contain a greater amount of short chain branching (>87%); the lower values of Tm also reflects this (see Tables 3 and 4).34,35 This would suggest that the steric hindrance provided by the difluorobenzhydryl groups likely inhibits extensive “chain-walking” and favors monomer insertion; the difference in run temperature may also be a contributing factor. It has been reported in previous experiments that higher polymerization temperatures result in more highly branched polyethylene.3b,5b,c,10b,24,26 Based on literature precedent, we propose the methyl branch is generated by a single chain walking step involving β-H elimination, a 2,1-reinsertion and then coordination/insertion of ethylene. In the current system, the steric hindrance imparted by the ortho-alkyl group inhibits further nickel migration to a more bulky secondary Ni-alkyl resulting in high levels of methyl branches. Unlike the results by Gao and co-workers,33e the presence of methyl branches was not accompanied by sizable amounts of long chain branching. Evidently, the current catalysts allow good control of the type of branch which will likely impact on the performance characteristics of these polyethylene materials (see later). Meanwhile, it is evident that the type of aluminum activator exerts some effect on the branching density of the polyethylene (EASC > Et2AlCl ∼ EtAlCl2) with EASC preferring to form more highly branched polyethylene. This finding is consistent with recent work in our group concerning EASC-activated α-diimino-nickel complexes in ethylene polymerization.8f
PE sample | T, °C | Tma, °C | Mwb | Xca, % | σbc, MPa | εb, % |
---|---|---|---|---|---|---|
a Determined by DSC; .b Determined by GPC, values ×105 g mol−1.c Determined by using a universal tester. | ||||||
PE-EtAlCl240Ni5 | 40 | 69.6 | 9.22 | 20.06 | 6.5 | 223 |
PE-EtAlCl250Ni5 | 50 | 50.1 | 8.88 | 13.60 | 4.0 | 413 |
PE-M40Ni5 | 40 | 68.0 | 8.67 | 22.40 | 10.06 | 366 |
PE-M50Ni5 | 50 | 63.1 | 7.44 | 16.96 | 5.41 | 405 |
PE-Et2AlCl40Ni5 | 40 | 77.3 | 8.36 | 16.30 | 5.62 | 211 |
PE-EASC40Ni5 | 40 | 73.8 | 8.29 | 15.71 | 4.60 | 382 |
Firstly, monotonic tensile stress–strain measurements were undertaken at room temperature with each test performed with three specimens in order to achieve concordant results; the stress–strain curves are depicted in Fig. 5. For the two samples prepared using EtAlCl2, PE-EtAlCl240Ni5 displayed the higher crystallinity (Xc = 20.06%), molecular weight (922 kg mol−1) and ultimate tensile strength (6.5 MPa), while the strain at break (223%) was lower. By comparison the maximum value of elongation at break was observed for PE-E50Ni5 (413%), while the level of crystallinity (Xc = 13.60%) and molecular weight (888 kg mol−1) were less. Similar observations were noted for the two samples prepared with Ni5/MAO, with PE-M40Ni5 showing the higher tensile stress [σb = 10.06 MPa], crystallinity [Xc = 22.4%] and molecular weight [Mw = 867 kg mol−1] but with the lower strain at break [εb = 366%]. Clearly the degree of crystallinity impacts on the mechanical properties of these polymers,36 with higher crystallinity leading to polyethylene displaying the highest ultimate tensile strength but the lower value of εb. Nonetheless, the variations in molecular weight of the polymers should also likely impact on these mechanical properties. Furthermore, by consideration of the four polymer samples obtained at 40 °C, it apparent that the type of aluminum co-catalyst also impacts on the mechanical properties with stress-at-break values ranging from 4.6 to 10.06 MPa and strain-at-break values ranging from 211% to 382%. As a final point, PE-M50Ni5 displayed a higher tensile stress and a reasonable elongation at break when compared with polymers obtained in previous work using nickel catalysts under similar conditions (i.e., MAO as activator, reaction temperature = 50 °C, PC2H4 = 10 atm and run time = 30 min).9a,b
Fig. 5 Stress–strain curves for samples, PE-EtAlCl240Ni5, PE-EtAlCl250Ni5, PE-M40Ni5, PE-M50Ni5, PE-Et2AlCl40Ni5 and PE-EASC40Ni5; the vertical line represents the breakage point. |
Secondly, the six polyethylene samples were subjected to stress–strain recovery tests by using dynamic mechanical analysis at 30 °C (Fig. S44†). Ten cycles were involved in each recovery test to allow for elastic extenuation, while the elastic recovery (R) was recorded at about 80% of the maximum tensile strength (σ); σ was also determined by using dynamic mechanical analysis. The stress–strain hysteresis loops showed constant recovery levels observed for all samples after the first cycle, which demonstrated that all samples possessed the characteristics of thermoplastic elastomers (TPE's). With an increase in the polymerization run temperature from 40 °C to 50 °C, the R value of the polymer generated using EtAlCl2 improved from 47.7% to 52.8%. Similarly, the elastic recovery of the sample produced using MAO increased from 46.1% to 48.0%. Evidently, this study of elastic recovery indicates that the run temperature also played an important role in the elastomeric properties of the polymer besides crystallinity. It is worth highlighting that the high molecular weight of the polymer samples described herein makes them unique when compared with previously reported polyethylenes with thermoplastic elastomer characteristics.5l,8c,8d,g,9a
Of particular note, Ni5 on activation with EASC showed the highest activity of 1.0 × 107 g of PE per (mol of Ni) per h at 40 °C, while the polyethylene displayed not only a high molecular weight but also a high degree of branching (102 branches/1000 carbons: % Me = 87.7). Moreover, mechanical tests performed on these branched polyethylenes highlighted the role played by crystallinity (Xc) and molecular weight (Mw) on the tensile strength (σb) and elongation at break (εb).
Footnote |
† Electronic supplementary information (ESI) available: NMR spectra of ligand compounds and complexes, GPC traces of polyethylenes, and crystal data and structure refinements along with X-ray crystallographic data. CCDC 2161608 (L1), 2161609 (Ni1) and 2161610 (Ni5). For ESI and crystallographic data in CIF or other electronic format see https://doi.org/10.1039/d2ra04321a |
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