Unsymmetrical Strategy on α-Diimine Nickel and Palladium Mediated Ethylene (Co)Polymerizations

Among various catalyst design strategies used in the α-diimine nickel(II) and palladium(II) catalyst systems, the unsymmetrical strategy is an effective and widely utilized method. In this contribution, unsymmetrical nickel and palladium α-diimine catalysts (Ipty/iPr-Ni and Ipty/iPr-Pd) derived from the dibenzobarrelene backbone were constructed via the combination of pentiptycenyl and diisopropylphenyl substituents, and investigated toward ethylene (co)polymerization. Both of these catalysts were capable of polymerizing ethylene in a broad temperature range of 0–120 °C, in which Ipty/iPr-Ni could maintain activity in the level of 106 g mol−1 h−1 even at 120 °C. The branching densities of polyethylenes generated by both nickel and palladium catalysts could be modulated by the reaction temperature. Compared with symmetrical Ipty-Ni and iPr-Ni, Ipty/iPr-Ni exhibited the highest activity, the highest polymer molecular weight, and the lowest branching density. In addition, Ipty/iPr-Pd could produce copolymers of ethylene and methyl acrylate, with the polar monomer incorporating both on the main chain and the terminal of branches. Remarkably, the ratio of the in-chain and end-chain polar monomer incorporations could be modulated by varying the temperature.

Among various catalyst design strategies, the unsymmetrical strategy has been applied extensively. To date, this strategy mainly has three operative manners: (1) different N-aryl substituents on the two sides of the α-diimine ligand; (2) different N-substituents involving nonaromatic groups on the two sides of the α-diimine ligand; and (3) different substituents on the 2,6-positions of one N-aryl ring. In the first manner of the unsymmetrical strategy, dibenzhydryl substituents have been utilized widely as one of the N-aryl moiety, coupling with another aryl group to build the α-diimine framework (Scheme 1, I). For example, Chen and coworkers reported a series of α-diimine palladium catalysts featuring the dibenzhydryl group and systematically steric demanding aryl rings [35]. These These catalysts were capable of modulating activities, polymer molecular weights and branching densities in a wide range. Sun [36][37][38], Dai [39][40][41], and our group [42] also independently developed distinctive unsymmetrical α-diimine nickel and palladium catalysts based on the dibenzhydryl substituent. Besides the dibenzhydryl type, various steric encumbering N-aryl substituents have been used in the unsymmetrical systems [43][44][45][46][47]. Recently, a flexible alkyl amine was introduced into the α-diimine ligand, replacing one bulky aryl amine moiety (Scheme 1, II) [48]. The resultant unsymmetrical nickel and palladium catalysts exhibited moderate to high activities, and afforded low to high molecular weight polyethylenes with varied branching densities. On the contrast to the former two ways that construct catalysts with unsymmetrical structures, the third method of the unsymmetrical strategy generally endows the catalyst a C2 symmetrical geometry (Scheme 1, III) [49][50][51][52][53][54], among which α-diimine nickel catalysts usually demonstrated excellent ethylene polymerization performance, enabling high activities, high molecular weights, as well as high thermal stability. Moreover, these catalysts also exhibited good catalytic behaviour toward α-olefin polymerization, such as propylene and 1-hexene. Recently, with further combination of the rotation-restricted strategy, benzosuberyl substituents were adopted in the unsymmetrical strategy, forming unsymmetrical structures rather than C2 symmetrical structures (Scheme 1, IV) [55,56]. For example, "sandwich-like" geometries were found in the α-diimine nickel catalysts, which generated polyethylenes with higher molecular weights than those of their free-rotated dibenzhydryl counterparts. Recently, our group has developed α-diimine nickel and palladium catalysts derived from a bulky dibenzobarrelene backbone and bulky axial pentiptycenyl substituents (Scheme 2, Ipty-Ni and Ipty-Pd) [10,[57][58][59]. These two catalysts could produce ultrahighly branched (>200/1000C) polyethylenes with exclusive methyl branches, of which the branching density generated by the palladium system could be modulated through a polar additive method. Based on these results, we attempted to apply the unsymmetrical strategy in this α-diimine system by replacing one of the pentiptycenyl substituents with the 2,6-diisopropyl-substituted phenyl group, which has been widely used in the catalyst modification [24,26,28,30,34]. Thus, in this contribution, unsymmetrical nickel (Ipty/ i Pr-Ni) and palladium (Ipty/ i Pr-Pd) α-diimine catalysts were synthesized, and further studied toward ethylene co(polymerization), which exhibited distinctive polymerization properties. Recently, our group has developed α-diimine nickel and palladium catalysts derived from a bulky dibenzobarrelene backbone and bulky axial pentiptycenyl substituents (Scheme 2, Ipty-Ni and Ipty-Pd) [10,[57][58][59]. These two catalysts could produce ultrahighly branched (>200/1000C) polyethylenes with exclusive methyl branches, of which the branching density generated by the palladium system could be modulated through a polar additive method. Based on these results, we attempted to apply the unsymmetrical strategy in this α-diimine system by replacing one of the pentiptycenyl substituents with the 2,6-diisopropyl-substituted phenyl group, which has been widely used in the catalyst modification [24,26,28,30,34]. Thus, in this contribution, unsymmetrical nickel (Ipty/ i Pr-Ni) and palladium (Ipty/ i Pr-Pd) α-diimine catalysts were synthesized, and further studied toward ethylene co(polymerization), which exhibited distinctive polymerization properties. These catalysts were capable of modulating activities, polymer molecular weights and branching densities in a wide range. Sun [36][37][38], Dai [39][40][41], and our group [42] also independently developed distinctive unsymmetrical α-diimine nickel and palladium catalysts based on the dibenzhydryl substituent. Besides the dibenzhydryl type, various steric encumbering N-aryl substituents have been used in the unsymmetrical systems [43][44][45][46][47]. Recently, a flexible alkyl amine was introduced into the α-diimine ligand, replacing one bulky aryl amine moiety (Scheme 1, II) [48]. The resultant unsymmetrical nickel and palladium catalysts exhibited moderate to high activities, and afforded low to high molecular weight polyethylenes with varied branching densities. On the contrast to the former two ways that construct catalysts with unsymmetrical structures, the third method of the unsymmetrical strategy generally endows the catalyst a C2 symmetrical geometry (Scheme 1, III) [49][50][51][52][53][54], among which α-diimine nickel catalysts usually demonstrated excellent ethylene polymerization performance, enabling high activities, high molecular weights, as well as high thermal stability. Moreover, these catalysts also exhibited good catalytic behaviour toward α-olefin polymerization, such as propylene and 1-hexene. Recently, with further combination of the rotation-restricted strategy, benzosuberyl substituents were adopted in the unsymmetrical strategy, forming unsymmetrical structures rather than C2 symmetrical structures (Scheme 1, IV) [55,56]. For example, "sandwich-like" geometries were found in the α-diimine nickel catalysts, which generated polyethylenes with higher molecular weights than those of their free-rotated dibenzhydryl counterparts.
Ar Recently, our group has developed α-diimine nickel and palladium catalysts derived from a bulky dibenzobarrelene backbone and bulky axial pentiptycenyl substituents (Scheme 2, Ipty-Ni and Ipty-Pd) [10,[57][58][59]. These two catalysts could produce ultrahighly branched (>200/1000C) polyethylenes with exclusive methyl branches, of which the branching density generated by the palladium system could be modulated through a polar additive method. Based on these results, we attempted to apply the unsymmetrical strategy in this α-diimine system by replacing one of the pentiptycenyl substituents with the 2,6-diisopropyl-substituted phenyl group, which has been widely used in the catalyst modification [24,26,28,30,34]. Thus, in this contribution, unsymmetrical nickel (Ipty/ i Pr-Ni) and palladium (Ipty/ i Pr-Pd) α-diimine catalysts were synthesized, and further studied toward ethylene co(polymerization), which exhibited distinctive polymerization properties.

Synthesis and Characterization of Ipty/ i Pr-Ni and Ipty/ i Pr-Pd
As shown in Scheme 3, the unsymmetrical α-diimine ligand Ipty/ i Pr-L was synthesized through a two-step procedure, in which the ketone-imine intermediate was first prepared. Treatments of Ipty/ i Pr-L with precursors NiBr 2 (DME) or PdMeCl(COD) produced the corresponding nickel dibromide complex Ipty/ i Pr-Ni or palladium methyl chloride Ipty/ i Pr-Pd in high yields, respectively. For comparison, symmetrical nickel complexes i Pr-Ni [60] and Ipty-Ni [10] were also prepared according to the reported literature.

Scheme 2.
The unsymmetrical strategy on the α-diimine nickel and palladium catalysts in this tribution.

Synthesis and Characterization of Ipty/ i Pr-Ni and Ipty/ i Pr-Pd
As shown in Scheme 3, the unsymmetrical α-diimine ligand Ipty/ i Pr-L was syn sized through a two-step procedure, in which the ketone-imine intermediate was first pared. Treatments of Ipty/ i Pr-L with precursors NiBr2(DME) or PdMeCl(COD) produ the corresponding nickel dibromide complex Ipty/ i Pr-Ni or palladium methyl chlo Ipty/ i Pr-Pd in high yields, respectively. For comparison, symmetrical nickel compl i Pr-Ni [60] and Ipty-Ni [10] were also prepared according to the reported literature. The new α-diimine ligand and the palladium complex were fully characterize 1 H and 13 C NMR spectroscopy, and elemental analysis, while the nickel complex was i tified by mass spectroscopy and elemental analysis. In addition, molecular structur Ipty/ i Pr-Ni and Ipty/ i Pr-Pd were further confirmed by X-ray diffraction analysis (Fig  1 and 2). Ipty/ i Pr-Ni displays a typical distorted tetrahedral geometry, in which the a between the N−Ni−N plane and the Br−Ni−Br plane is 87.43°, smaller than that of Ipt (90.00°) [58]. Moreover, the twist angle between the pentiptycene aryl ring and the n diamine (N−Ni−N) plane is 78.77°, smaller than that of 84.25° in Ipty-Ni. This result gests that the repulsive interaction between the dibenzobarrelene backbone and pentiptycene substituent in Ipty/ i Pr-Ni is larger than that in Ipty-Ni, which could lea a more crowded environment around the nickel centre. The larger buried volume (47.8%) of Ipty/ i Pr-Ni ( Figure 3) than that (42.3%) of Ipty-Ni further verifies this antic tion. In comparison with i Pr-Ni, the twist angle between the 2,6-diisopropyl phenyl and the N−Ni−N plane in Ipty/ i Pr-Ni is slightly larger (82.86° vs. 82.45°), indicative slightly larger steric hindrance. For the nickel complexes, the order of the buried vol is Ipty/ i Pr-Ni (Vbur = 47.8%) > i Pr-Ni (Vbur = 45.3%) > Ipty-Ni (Vbur = 42.3%) [60]. For p dium analogues, the steric bulk also follows the order of Ipty/ i Pr-Pd > i Pr-Pd > Ipty (Vbur = 50.8% vs. 49.4% vs. 44.6%). In addition, it is obvious that in the solid-state struct of both Ipty/ i Pr-Ni and Ipty/ i Pr-Pd, the rigid dibenzobarrelene backbone provides a fective shield on the back side of the metal centre, which could retard the associative c transfer or chain transfer to monomer [28]. The new α-diimine ligand and the palladium complex were fully characterized by 1 H and 13 C NMR spectroscopy, and elemental analysis, while the nickel complex was identified by mass spectroscopy and elemental analysis. In addition, molecular structures of Ipty/ i Pr-Ni and Ipty/ i Pr-Pd were further confirmed by X-ray diffraction analysis (Figures 1 and 2). Ipty/ i Pr-Ni displays a typical distorted tetrahedral geometry, in which the angle between the N−Ni−N plane and the Br−Ni−Br plane is 87.43 • , smaller than that of Ipty-Ni (90.00 • ) [58]. Moreover, the twist angle between the pentiptycene aryl ring and the nickel diamine (N−Ni−N) plane is 78.77 • , smaller than that of 84.25 • in Ipty-Ni. This result suggests that the repulsive interaction between the dibenzobarrelene backbone and the pentiptycene substituent in Ipty/ i Pr-Ni is larger than that in Ipty-Ni, which could lead to a more crowded environment around the nickel centre. The larger buried volume V bur (47.8%) of Ipty/ i Pr-Ni ( Figure 3) than that (42.3%) of Ipty-Ni further verifies this anticipation. In comparison with i Pr-Ni, the twist angle between the 2,6-diisopropyl phenyl ring and the N−Ni−N plane in Ipty/ i Pr-Ni is slightly larger (82.86 • vs. 82.45 • ), indicative of a slightly larger steric hindrance. For the nickel complexes, the order of the buried volume is Ipty/ i Pr-Ni (V bur = 47.8%) > i Pr-Ni (V bur = 45.3%) > Ipty-Ni (V bur = 42.3%) [60]. For palladium analogues, the steric bulk also follows the order of Ipty/ i Pr-Pd > i Pr-Pd > Ipty-Pd (V bur = 50.8% vs. 49.4% vs. 44.6%). In addition, it is obvious that in the solid-state structures of both Ipty/ i Pr-Ni and Ipty/ i Pr-Pd, the rigid dibenzobarrelene backbone provides an effective shield on the back side of the metal centre, which could retard the associative chain transfer or chain transfer to monomer [28].

Ethylene Polymerizaiton by Ipty/ i Pr-Ni
The catalytic properties of Ipty/ i Pr-Ni were first investigated toward the effect of cocatalysts, wherein three aluminium activators (MMAO, MAO, and AlEt 2 Cl) were selected to carry out ethylene polymerization at 50 • C (Table 1). Among these three aluminium agents, the activation of MMAO endowed Ipty/ i Pr-Ni the highest activity of 6.96 × 10 6 g mol −1 h −1 , along with a high molecular weight that was only slightly lower than the highest value achieved by MAO (1417 kDa vs. 1503 kDa). Moreover, the effect of MMAO and MAO on the branching density was negligible. Compared to MMAO and MAO, Et 2 AlCl had a preference for obtaining higher branching number (86/1000C), yet the polymer molecular weight sharply dropped ( Table 1, entries 3 vs. 1, 2). Taking the activity and the molecular weight into consideration, MMAO was selected as the activator in further studies of Ipty/ i Pr-Ni catalytic performance toward ethylene polymerization ( Table 2). In a broad temperature range of 0-120 • C, Ipty/ i Pr-Ni displayed excellent ethylene polymerization activities in the level of 10 6 -10 7 g mol −1 h −1 ( Table 2, entries 1-6). With the temperature increasing, the activity ascended first, reaching the highest value of 1.43 × 10 7 g mol −1 h −1 at 30 • C that is comparable to that of classical metallocene catalysts, and then descended. We assume that the initiation of Ipty/ i Pr-Ni is incomplete at the low temperature of 0 • C, while the catalyst deactivation is attributed to the decrease in activities at higher temperatures. Note that although the activity dropped at 120 • C, it remained in the level of 10 6 g mol −1 h −1 ( Table 2, entry 6). In terms of the polymer molecular weight, a descending tendency was observed with the temperature increasing. This could be ascribed to the acceleration of chain transfer associated with β-H elimination, which was the outcome of the decreasing axial steric hindrance caused by the faster rotation of the N-aryl rings at elevated temperature. Furthermore, the increased β-H elimination by chain transfer could also enhance the probability of chain walking, leading to the increase in the branching density. As a result, the variation of polyethylene microstructures from a lightly branched (16/1000C) semi-crystalline structure (T m = 111.9 • C) to a highly branched (105/1000C) amorphous structure was able to be modulated by changing the reaction temperature.
To study the polymerization medium influence on the catalytic and polymer properties, hexane was used under the condition of 50 • C. Compared to those in toluene, the activity and the polymer molecular weight in hexane were enhanced by about 1.63 and 1.43 times, respectively, while the branching density decreased (Table 1, entries 7 vs. 3). It is assumed that the metal cation and the cocatalyst anion interaction is weakened in the hexane [61], rendering the nickel centre more electrophilic [62]. In consequence, ethylene coordination and insertion as the rate-limiting step in α-diimine nickel mediated ethylene polymerization is facilitated to achieve a higher activity. Moreover, the relatively fast ethylene coordination and insertion relative to chain transfer and chain walking could also be responsible for the increase in the molecular weight and the decrease in the branching density.  Figure 4). Generally, the increase in the steric hindrance around the metal centre is in disadvantage of ethylene coordination, as well as β-H elimination. The former will result in the decrease in the activity, while the latter can improve the polymer molecular weight and lower the branching density. However, as for these three nickel catalysts, the tendency on activity was Ipty/ i Pr-Ni > i Pr-Ni > Ipty-Ni, in line with the steric bulk order of Ipty/ i Pr-Ni > i Pr-Ni > Ipty-Ni, which did not fit the general rule. In view of the polymer molecular weight, the trend followed the order of Ipty/ i Pr-Ni > i Pr-Ni > Ipty-Ni, in agreement with the increasing steric hindrance tendency. Note that the molecular weight of polyethylenes obtained by Ipty/ i Pr-Ni was dramatically higher than those of i Pr-Ni and Ipty-Ni. Furthermore, the branching density showed an upward trend (Ipty/ i Pr-Ni < i Pr-Ni < Ipty-Ni), consistent with the decrease in chain walking associated with the reduced β-H elimination.
To study the polymerization medium influence on the catalytic ties, hexane was used under the condition of 50 °C. Compared to activity and the polymer molecular weight in hexane were enhanc 1.43 times, respectively, while the branching density decreased (Tab is assumed that the metal cation and the cocatalyst anion interactio hexane [61], rendering the nickel centre more electrophilic [62]. In c coordination and insertion as the rate-limiting step in α-diimine nick polymerization is facilitated to achieve a higher activity. Moreover, t ylene coordination and insertion relative to chain transfer and chai be responsible for the increase in the molecular weight and the decr density. Parallel ethylene polymerization experiments of symmetrical i 30 °C were performed (Table 1, entries 8, 9 vs. 2). Under otherwise unsymmetrical Ipty/ i Pr-Ni exhibited the highest activity and polym ( Figure 4). Generally, the increase in the steric hindrance around t disadvantage of ethylene coordination, as well as β-H elimination. T in the decrease in the activity, while the latter can improve the polym and lower the branching density. However, as for these three nick dency on activity was Ipty/ i Pr-Ni > i Pr-Ni > Ipty-Ni, in line with th Ipty/ i Pr-Ni > i Pr-Ni > Ipty-Ni, which did not fit the general rule. In molecular weight, the trend followed the order of Ipty/ i Pr-Ni > i Pr-N ment with the increasing steric hindrance tendency. Note that the polyethylenes obtained by Ipty/ i Pr-Ni was dramatically higher tha Ipty-Ni. Furthermore, the branching density showed an upward tre Ni < Ipty-Ni), consistent with the decrease in chain walking associa β-H elimination.

Copolymerizaiton of Ethylene and Polar Monomer by Ipty/ i Pr-Ni
Ipty/ i Pr-Ni was further investigated toward the ethylene copol bio-renewable monomer methyl 10-undecenoate (UA) [63] in the act

Copolymerizaiton of Ethylene and Polar Monomer by Ipty/ i Pr-Ni
Ipty/ i Pr-Ni was further investigated toward the ethylene copolymerization with the bio-renewable monomer methyl 10-undecenoate (UA) [63] in the activation of MMAO. In the presence of 0.05 M of UA, Ipty/ i Pr-Ni showed a high copolymerization activity of 6.3 × 10 5 g mol −1 h −1 , accompanied with a high molecular weight (443 kDa) and the incorporation ratio of 0.12 mol% (Table 3, entry 1). When the concentration of UA was increased to 0.1 M, the comonomer incorporation was marginally improved to 0.18 mol%, while the activity and the copolymer molecular weight slightly decreased (Table 3, entry 2). To further improve the comonomer incorporation, ethylene pressure was reduced from 8 bar to 6 bar to 2 bar (Table 3, entries 3 and 4). At the low ethylene pressure of 2 bar, the comonomer incorporation reached 0.41 mol%, yet the activity and the copolymer molecular weight sharply dropped, as anticipated.

Mechanical Properties of (Co)Polymers Generatedr by Ipty/ i Pr-Ni
Three polyethylene samples with different branching densities were selected for tensile tests to investigate the mechanical properties (Figure 5a). Stress at break values of the three selected polyethylenes followed an opposite tendency (5.9 MPa > 4.5 MPa > 2.3 MPa) to the variation of the branching density (71/1000C < 81/1000C < 94/1000C). Strain at break values were observed in the range of 239% to 266%. For comparison, one copolymer sample with lower branching density was chosen for the mechanical study. Values of stress at break and strain at break were improved dramatically to 9.1 MPa and 470%, respectively. Moreover, the strain recovery of the selected copolymer showed a value of 51%, indicating the feature of elastomer (Figure 5b).

Ethylene Polymerizaiton by Ipty/ i Pr-Pd
In the presence of sodium tetrakis(3,5-bis(trifluoromethyl)phenyl)borate (NaBArF), Ipty/ i Pr-Pd could also catalyse ethylene polymerization in the broad temperature range of 0-120 • C (Table 4). Compared to the nickel analogue, the activity and the molecular weight exhibited similar trends with the temperature increasing, of which the activity rose first, and then fell, while the polymer molecular weight decreased. On the contrast, the branching density displayed a decreasing tend along with the elevated temperature. This phenomenon was in agreement with our previous reported Ipty-Pd [10], yet inconsistent with the general fact that the branching density in the α-diimine palladium systems is independent with the reaction temperature [64]. According to the previous report by Brookhart, one plausible explanation is that the activation entropy of ethylene insertion into a secondary Pd-alkyl bond is much more negative than that into a primary Pd-alkyl bond [65]. More importantly, highly branched (124-164/1000C) structures of polyethylenes were found, which is rare in the α-diimine palladium catalysts. The relationship of the branching density and ethylene pressure was studied by lowering ethylene pressure (Table 4,  to the variation of the branching density (71/1000C < 81/1000C < 94/1000C). Strain a values were observed in the range of 239% to 266%. For comparison, one copolyme ple with lower branching density was chosen for the mechanical study. Values of s break and strain at break were improved dramatically to 9.1 MPa and 470%, respec Moreover, the strain recovery of the selected copolymer showed a value of 51%, ind the feature of elastomer (Figure 5b).

Ethylene Polymerizaiton by Ipty/ i Pr-Pd
In the presence of sodium tetrakis(3,5-bis(trifluoromethyl)phenyl)borate (Na Ipty/ i Pr-Pd could also catalyse ethylene polymerization in the broad temperature of 0-120 °C (Table 4). Compared to the nickel analogue, the activity and the mo weight exhibited similar trends with the temperature increasing, of which the activi

Copolymerizaiton of Ethylene and Polar Monomer by Ipty/ i Pr-Pd
The catalytic properties of Ipty/ i Pr-Pd toward the copolymerization of ethylene and methyl acrylate (MA) were investigated at various temperatures and comonomer concentrations (Table 5). By employing 1.0 M MA and the radical inhibitor galvinoxyl, the activity went up first, and then fell with the increase in temperature from 30 • C to 90 • C, as well as the copolymer molecular weight ( Table 5, entries 1-4). The MA incorporation increased with the elevated temperature, reaching the highest value of 1.98 mol% at 90 • C, while the branching density showed a descending tend, similar to the situation in ethylene polymerization. Under otherwise identical conditions, the variation of comonomer concentration from 0.5 M to 1.0 M to 2.0 M resulted in the increase in MA incorporation (up to 2.21 mol%), yet at the cost of the activity and the copolymer molecular weight, as anticipated (Table 5, entries 3, 5 vs. 6). Moreover, highly branched architectures were formed in the Ipty/ i Pr-Pd-catalysed copolymerization of ethylene and MA.
Typically, the acrylate groups at the terminal of branches (T MA ) dominate in the structures of copolymers generated by α-diimine palladium catalysts because of chain walking. Ipty-Pd [10] and two other palladium catalysts [15,27] have been reported as rare examples that produced highly branched copolymers featuring very high ratio of acrylate groups on the main chain (M MA ), which is ascribed to the 1,2-insertion of MA. Compared to Ipty-Pd, the highly branched copolymers afforded by Ipty/ i Pr-Pd also preferred inchain acrylate units. As shown in Figure 6 [15,27]. Note that the ratio of M MA and T MA generated by Ipty/ i Pr-Pd could be modulated by varying the reaction temperature (Table 5, entries 1-4), in contrast with the slight change in the ratio in the Ipty-Pd system. At low temperature of 30 • C, the in-chain incorporation of MA was overwhelming favoured over the end-chain incorporation, with a ratio of 92:8 (Table 5, entry 1). With the temperature increasing, the proportion of the in-chain acrylate incorporation gradually dropped, reaching a similar value to that of the end-chain incorporation at 90 • C (53:47). We speculated that the replacement of one pentiptycenyl substituent with an isopropyl-substituted phenyl group changed the rigid environment of the palladium catalyst, eventually reducing the selectivity of 1,2-insertion. In addition, the comonomer concentration exerted a negligible influence on the comonomer insertion pathway (Table 5, entries 5, 6 vs. 3).  Typically, the acrylate groups at the terminal of branches (TMA) dominate in th tures of copolymers generated by α-diimine palladium catalysts because of chain w Ipty-Pd [10] and two other palladium catalysts [15,27] have been reported as rare ples that produced highly branched copolymers featuring very high ratio of a groups on the main chain (MMA), which is ascribed to the 1,2-insertion of MA. Com to Ipty-Pd, the highly branched copolymers afforded by Ipty/ i Pr-Pd also prefer chain acrylate units. As shown in Figure 6, 13 C NMR spectroscopy revealed chara signals for MMA units (177.24 ppm and 51.42 ppm), and TMA units (174.45 ppm an ppm) [15,27]. Note that the ratio of MMA and TMA generated by Ipty/ i Pr-Pd could b ulated by varying the reaction temperature ( Table 5, entries 1-4), in contrast w slight change in the ratio in the Ipty-Pd system. At low temperature of 30 °C, the i incorporation of MA was overwhelming favoured over the end-chain incorporatio a ratio of 92:8 (Table 5, entry 1). With the temperature increasing, the proportion o chain acrylate incorporation gradually dropped, reaching a similar value to tha end-chain incorporation at 90 °C (53:47). We speculated that the replacement pentiptycenyl substituent with an isopropyl-substituted phenyl group changed th environment of the palladium catalyst, eventually reducing the selectivity of 1,2-in In addition, the comonomer concentration exerted a negligible influence on the co mer insertion pathway (Table 5, Table 5, entries 1-4) in the 13 C NMR spectra (500 MHz, 293 K, CDCl 3 ) of ethylene-MA copolymers.

General Information
All syntheses involving air-and moisture sensitive compounds were carried out using standard Schlenk-type glassware (or in a glove box) under an atmosphere of nitrogen. All solvents were purified from the MBraun SPS system. NMR spectra for the ligand, complexes, and polymers were recorded on a Bruker AV400 ( 1 H: 400 MHz, 13  Materials: 9,10-dihydro-9,10-ethanoanthracene-11,12-dione [66] and pentiptycene aminophenol [67] were prepared using the literature procedures. All other reagents were commercially available from Energy Chemical or Shanghai Titan Scientific Co, Ltd, and used as received.

Synthesis of Pentiptycene Aminoanisole
To a solution of pentiptycene aminophenol (3 g, 6.5 mmol) in 100 mL dry DMF at room temperature was added NaH (468 mg, 19.5 mmol) under nitrogen. After the bubbling ceased, CH 3 I (0.6 mL, 9.75 mmol) was added, and the mixture was stirred for 24 h. The reaction was quenched by adding 400 mL of distilled water, and then the aqueous layer was extracted with 3 × 50 mL of CH 2 Cl 2 . The combined organic phase was washed with 3 × 50 mL of distilled water and 50 mL of brine, and then was separated and dried with sodium sulphate. After evaporation of the solvent, the pure product was obtained as a white solid (2.6 g, 84.1% yield). 1

Synthesis of the Nickel Catalyst Ipty/ i Pr-Pd
To a solution of Ipty/ i Pr-L (250 mg, 0.294 mmol) in dry dichloromethane (25 mL) was added 81.8 mg (0.308 mmol) of PdMeCl(COD). After stirring the mixture for 2 days at room temperature, the solvent was evaporated under reduced pressure. The desired compound can be isolated from repeated recrystallized from n-hexane and dichloromethane, and was obtained as an orange solid (220 mg, 74.2% yield). 1

X-ray Diffraction
All data collections were performed at 293 K on a Bruker SMART APEX diffractometer with a CCD area detector, using graphite-monochromated Mo Kα radiation (λ = 0.71073 Å) or Cu Kα radiation (λ = 1.54178 Å). The determination of crystal class and unit cell parameters was carried out by the SMART program package [68]. The raw frame data were processed using SAINT and SADABS to yield the reflection data file [69]. All structures were solved by direct methods and refined by full-matrix least-squares procedures on F 2 using SHELXTL or Olex2 [70,71]. Refinement was performed on F 2 anisotropically for all non-hydrogen atoms by the full-matrix least-squares method. The hydrogen atoms were placed at the calculated positions and were included in the structure calculation without further refinement of the parameters. Exceptions and special features: For Ipty/ i Pr-Ni, the BASF/TWIN refinement was performed to obtain the reasonable Flack x. The program SQUEEZE [72] was used to remove mathematically the effect of the solvent. The quoted formula and derived parameters are not included the squeezed solvent molecules. For Ipty/ i Pr-Pd, the BASF/TWIN refinement was performed to obtain the reasonable Flack x. The program SQUEEZE [72] was used to remove mathematically the effect of the solvent. The quoted formula and derived parameters are not included the squeezed solvent molecules.

A General Procedure for Ethylene Polymerization
In a typical experiment, a 350 mL glass pressure reactor connected with a high-pressure gas line was firstly dried at 90 • C under vacuum for at least 1 h. The reactor was then adjusted to the desired polymerization temperature. 98 mL of toluene and the cocatalyst were added to the reactor under N 2 atmosphere, and then the desired amount of the catalyst in 2 mL of CH 2 Cl 2 was injected into the polymerization system via syringe. With a rapid stirring, the reactor was pressurized and maintained at the desired ethylene pressure. After the desired reaction time, the pressure reactor was vented, and the polymerization was quenched via the addition of 100 mL EtOH (for the nickel system: acidic EtOH containing 5% HCl), filtered and dried in a vacuum oven to the constant weight.

A General Procedure for the Copolymerization of Ethylene with Polar Monomer
In a typical experiment, a 150 mL glass pressure reactor connected with a high-pressure gas line was firstly dried at 90 • C under vacuum for at least 1 h. The reactor was then adjusted to the desired polymerization temperature. 20 mL of toluene with the cocatalyst and polar monomer was added to the reactor under N 2 atmosphere, then the desired amount of the catalyst in 2 mL of CH 2 Cl 2 was injected into the polymerization system via syringe subsequently. With a rapid stirring, the reactor was pressurized and maintained at desired ethylene pressure. After the desired reaction time, the pressure reactor was vented, and the polymerization was quenched via the addition of 20 mL EtOH (for the nickel system: acidic EtOH containing 5% HCl), filtered and dried in a vacuum oven to the constant weight.

Conclusions
With the combination of the pentiptycenyl and diisopropylphenyl substituents, the unsymmetrical α-diimine nickel and palladium complexes (Ipty/ i Pr-Ni and Ipty/ i Pr-Pd) were constructed. In the activation of MMAO, Ipty/ i Pr-Ni exhibited excellent activities toward ethylene polymerization in a broad temperature range of 0-120 • C. Remarkably, the activity in the level of 10 6 g mol −1 h −1 was accessible even at high temperature of 120 • C. High molecular weight polyethylenes with variable branching density were accessible by varying the reaction temperature. Therefore, polyethylenes could convert from the lightly branched semi-crystalline structure to the highly branched amorphous structure. Compared to symmetrical Ipty-Ni and i Pr-Ni, unsymmetrical Ipty/ i Pr-Ni displayed much higher ethylene polymerization activity and molecular weight of polyethylenes, yet with the lowest branching density. Moreover, Ipty/ i Pr-Ni could copolymerize ethylene and methyl 10-undecenoate. As for Ipty/ i Pr-Pd, the broad temperature range of 0-120 • C was also applicable for ethylene polymerization. Polyethylenes with ultrahigh branching densities were obtained, and more importantly, the branching density could be modulated through changing the reaction temperature. In the copolymerization of ethylene and methyl acrylate, highly branched copolymers were afforded, with the acrylate units locating on both the main chain and the terminal of branches. In-chain acrylate incorporation dominated at low temperature of 30 • C, and the ratio of in-chain and end-chain incorporations could be modulated by the reaction temperature. This work shows an unsymmetrical strategy as an effective tool for modulating olefin polymerization.

Data Availability Statement:
The data presented in this study are available in this article.