Muhammad Zada1,2, Arumugam Vignesh1, Liwei Guo1,3, Randi Zhang1,2, Wenjuan Zhang3, Yanping Ma1, Yang Sun1, Wen-Hua Sun1,2,4. 1. Key Laboratory of Engineering Plastics and 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. Beijing 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. 4. Key Laboratory of High-Performance Synthetic Rubber and Its Composite Materials, Changchun Institute of Applied Chemistry, Chinese Academy of Sciences, Changchun 130022, China.
Abstract
A series of 2-((arylimino)ethyl)pyridine derivatives (L1-L5), each containing N-2,4-bis(dibenzocycloheptyl) groups with variations in the steric/electronic properties of the ortho-substituent in the aryl ring, and the corresponding nickel bromide precatalysts [2-N{2,4-(C15H13)-6-R-C6H2}C7H7N]NiBr2 (R = Me (Ni1), Et (Ni2), i-Pr (Ni3), Cl (Ni4), or F (Ni5)), have been prepared in high yield. All the precatalysts are air-stable and characterized by Fourier transform infrared spectroscopy and elemental analysis. The molecular structures of Ni2 and Ni5 were proved through single-crystal X-ray diffraction analysis. The steric/electronic impact of the catalysts on ethylene polymerization and the resulting polymer properties were studied. Upon activation with either MAO or EASC, all the complexes displayed higher activities (up to 7.93 × 106 g of PE (mol of Ni)-1 h-1 with MAO) in ethylene polymerization and produced moderate to highly branched unsaturated polyethylene with a molecular weight of up to 16.55 kg/mol with narrow dispersities (1.6-2.4). Significantly, the generated polyethylenes are branched and unsaturated with a major class of internal double bond (-CH=CH-) as compared to the terminal double bond (-CH=CH2) (vinylene/vinyl = 9.8:1 to 1.8:1). Notably, their catalytic activities, types of unsaturation, and branches are highly affected by the nature of the ortho-substituent and reaction temperature. Moreover, the precatalysts Ni4 and Ni5 (with N-ortho = Cl and F) exhibited lower catalytic activities, produced low-molecular-weight polyethylene with a high melt temperature and the least number of branches with an increased level of terminal double bonds.
A series of 2-((arylimino)ethyl)pyridine derivatives (L1-L5), each containing N-2,4-bis(dibenzocycloheptyl) groups with variations in the steric/electronic properties of the ortho-substituent in the aryl ring, and the corresponding nickelbromide precatalysts [2-N{2,4-(C15H13)-6-R-C6H2}C7H7N]NiBr2 (R = Me (Ni1), Et (Ni2), i-Pr (Ni3), Cl (Ni4), or F (Ni5)), have been prepared in high yield. All the precatalysts are air-stable and characterized by Fourier transform infrared spectroscopy and elemental analysis. The molecular structures ofNi2 and Ni5 were proved through single-crystal X-ray diffraction analysis. The steric/electronic impact of the catalysts on ethylenepolymerization and the resulting polymer properties were studied. Upon activation with either MAO or EASC, all the complexes displayed higher activities (up to 7.93 × 106 g of PE (mol ofNi)-1 h-1 with MAO) in ethylenepolymerization and produced moderate to highly branched unsaturated polyethylene with a molecular weight of up to 16.55 kg/mol with narrow dispersities (1.6-2.4). Significantly, the generated polyethylenes are branched and unsaturated with a major class of internal double bond (-CH=CH-) as compared to the terminal double bond (-CH=CH2) (vinylene/vinyl = 9.8:1 to 1.8:1). Notably, their catalytic activities, types of unsaturation, and branches are highly affected by the nature of the ortho-substituent and reaction temperature. Moreover, the precatalysts Ni4 and Ni5 (with N-ortho = Cl and F) exhibited lower catalytic activities, produced low-molecular-weight polyethylene with a high melt temperature and the least number of branches with an increased level of terminal double bonds.
Since the 1990s, the
effective design of a nickel precatalyst for
ethylenepolymerization has been the subject ofcontinued investigations.[1] Especially, broad branching contents of the obtained
polyethylenes, because of the propensity of the catalysts with facile
“chain walking”, led to producing promising materials
with a wide range of applications.[2] Structural
modifications ofcatalysts have been explored, which include the diazabutadiene-class
ofcomplexes[3] and other nickelcomplexes
in which the steric and electronic effects of the ligand backbone,
as well as the N-aryl substituents, played a vital
role in the catalytic performance and polymer properties.[4] An early example of a nickel precatalyst bearing
pyridine-based ligand framework (A, Chart ),[5] in which the steric hindrance at the ortho-position of the N-aryl ring played a significant role, leading to produce
mono and dinuclear complexes and showed high activity for ethylenepolymerization. The catalytic activity has been influenced by variations
in the pyridine moiety using methyl or mesityl in nickel precatalysts
for ethylenepolymerization (B, Chart ),[6] and generated
high molecular weight polyethylene with narrow dispersities and a
high degree of branches. Over the past several years, our group has
developed several effective cycloalkyl-fused pyridinyl–nickelcomplexes for ethylenepolymerization.[7] It has been observed that variations in the N-aryl
ring particularly using the electron-withdrawing groups at the para
position showed an enhanced effect on the catalytic activity for ethylenepolymerization, producing low-molecular-weight-branched polyethylene
with narrow dispersities.[8] Furthermore,
the incorporation ofdibenzhydryl substituents into the N-naphthyl ring (CChart )[4l,4m] led to enhanced catalytic activity
and generated low-molecular-weight polyethylene with narrow dispersities.
Meanwhile, highly active and thermally stable nickel precatalysts
have been investigated for ethylenepolymerization and produced materials
of semicrystalline nature in the range of ultrahigh molecular weight.[9] It has been recognized that the ortho-substituents
in the 2-(arylimino)pyridine-nickel and palladium precatalysts could
also be important for catalytic performance, thermal stability, and
polymer properties.[10] With this view, the
nickelcomplexes (D and E, Chart )[4k] bearing dibenzhydryl substituents at the 2,4-positions of the N-aryl ring have been investigated for ethylenepolymerization.
These complexes exhibited high catalytic activity and produced highly
branched polyethylene with narrow molecular weight distributions.
Similarly, the 2,4-fluorenyl substituents in the N-aryl ring proved substantial (F, Chart )[11] and produced
high molecular weight polyethylene with moderate to broad polydispersities.
However, the incorporation ofcycloalkyl groups into the N-aryl group showed slightly lower activity and produced low-molecular-weight
polyethylene.[7b] More recently, we have
developed 8-(arylimino)-5,6,7-trihydroquinoline-nickel precatalysts
for ethylenepolymerization and generated branched polyethylene ofvinyl/vinylenefunctionalities with narrow dispersities; such unsaturated
polymer materials highly demanded further functionalization.[12]
Chart 1
Development of 2-(Arylimino)pyridine-nickel(II)
Halide Precatalysts
Bearing Modified N-Aryl Substituted via Benzhydryl,
Fluorenyl, and Dibenzocycloheptyl Groups (A–G).
In the present work, we are developing dibenzocycloheptyl
groups
as the counterpart ofdibenzhydryl groups in D and E or fluorenyl groups in F (Chart ); we assumed that the steric
effect, as well as acidity of methine protons in 2,4-bis(dibenzhydryl)-6-R-imine
and 2,4-bis(fluorenyl)-6-methyl-iminealong with variable steric/electronic
properties of the ortho-position near the centralmetal may have some
influence on the catalytic performance and polymer properties.[13] In this regard, we report 2-(2,4-bis(dibenzocycloheptyl-6-R-phenylimino)ethyl)pyridine-nickel
precatalysts (G, Chart ), where R = Me, Et, i-Pr, Cl, and
F. The influence of the steric and electronic properties of the ortho-substituent
was investigated and then catalytic evaluation of G was
investigated in depth that is how the co-catalyst as well as reaction
parameters can impact the catalytic performance and properties of
the resulting polyethylene. Additionally, nearly related D, E, and F of the reported and current G precatalysts are also compared.
Results and Discussion
Synthesis
and Characterization
Using the Friedel–Crafts
alkylation reaction, five examples ofanilines (A1–A5) such as 2,4-(C15H13)-6-R-C6H2NH2 {R = Me (A1), Et (A2), i-Pr (A3), Cl (A4),
and F(A5)} were prepared and reasonable yield was obtained
(Scheme S1). The condensation reactions
of the respective aniline (A1–A5) with 1 M equivalent
ofacetylpyridine offered a series of ligands 2-N{2,4-(C15H13)-6-RC6H2}C7H7N {R = Me (L1), Et (L2), i-Pr (L3), Cl (L4), or F (L5)} as a yellow powder in 56–86% yield (Scheme ). All the ligands were characterized
by Fourier transform infrared (FT-IR), 1H, and 13CNMR spectroscopy as well as by elemental analysis. Treatment of
ligands (L1–L5) with (DME)NiBr2 (DME
= 1,2-dimethoxyethane) in a mixture ofethanol and dichloromethane
at room temperature afforded the corresponding nickel(II) bromidecomplexes (Ni1–Ni5) as a green powder in good
yield (82–95%). All these complexes were air-stable and characterized
by FT-IR spectroscopy and elemental analysis, as well as single-crystal
X-ray diffraction analysis for Ni2 and Ni5.
Scheme 1
Synthesis of Iminopyridine Ligands (L1–L5) and
Their Corresponding Nickel(II) Bromide Complexes (Ni1–Ni5)
In the FT-IR spectra of the
complexes, the absorption bands for
ν(C=N) shifted to lower wavenumbers of 1627–1621
cm–1 compared to their corresponding free ligands
(L1–L5) in the range of 1645–1634 cm–1, such shifts toward lower wavenumbers reveal the
effective coordination between the donor nitrogen atom of the ligand
framework and the metalcenter.[4k,4m,5,8a,9,11,12] The elemental
analysis results were consistent with the results of the prepared
compounds. Moreover, single-crystals ofNi2 and Ni5 suitable for X-ray determination were grown by slow diffusion
ofheptane into a solution of the respective complex in dichloromethane
at room temperature. During our attempt to growing the crystals, we
obtained the bis-ligated Ni2(a) and 2Ni5·HO as the dinuclear complex.
The images of the corresponding structures are shown in Figures and 2, respectively; their selected bond lengths and angles are collected
in Table . As shown
in Figure , the structure
of the biligated Ni2(a) complex can be best described
as distorted square-pyramidal geometry around the nickelcenter comprising
four chelating nitrogen atoms (N(1), N(2), N(1a), and N(2a)) of the
two ligands, one bromide (Br(1)), the other bromide (Br(2)) acting
as a free-anion, similar findings have been reported using bis(2-((2,4-dibenzohydryl-6-ethylphenylimino)pyridyl
nickelbromidecomplexes.[4k] In addition,
each ligand forms five-membered heterocyclic rings around the nickelcenter as Ni(1), N(1), C(5), C(6), and N(2) and Ni(1), N(1a), C(5)a,
C(6a), and N(2a), in which the atoms C(5) and C(6) deviate (0.139–0.44
Å) versus C(5a) and C(6a) (0.169–0.242 Å) from the
coplane of atoms Ni(1), N(1), and N(2) versus Ni(1), N(1a), and N(2a),
respectively. The Ni(1) atom deviates by 0.187 or 0.275 Å from
the coplane of atoms N(1), C(5), C(6), and N(2) or N(1a), C(5a), C(6a),
and N(2a), respectively. Moreover, the plane of bidentate nitrogen
atoms was alongside the nickelcenter and the N-aryl
plane is nearly perpendicular with a dihedral angle of 85.51°,
similar observations have been reported in the literature for 2-aryliminopyridylnickel
analogs.[2d,4d,4k−4m,5,7c] The
bond length ofNi(1)–N(1)pyridine (2.039(4) Å)
is slightly shorter than the bond length ofNi(1)–N(2)imine (2.059(4) Å), highlighting more effective coordination
of the pyridinenitrogen atom compared to the iminenitrogen atom,
which is consistent with the reported literature.[4k−4m,5,8b,9−12]
Figure 1
ORTEP
diagram of bis-ligated Ni2(a) with thermal ellipsoids
shown at a probability level of 30%. All the hydrogen atoms have been
omitted for clarity.
Figure 2
ORTEP diagram of 2Ni5·HO with thermal
ellipsoids shown at a probability level
of 30%. All the hydrogen atoms have been omitted for clarity.
Table 1
Selected Bond Lengths (Å) and
Angles (deg) of Ni2(a) and 2Ni5·HO
Ni2(a)
2Ni5·H2O
Bond Lengths (Å)
Ni(1)–N(1)
2.039(4)
Ni(1)–N(1)
2.042(3)
Ni(1)–N(2)
2.059(4)
Ni(1)–N(2)
2.102(3)
Ni(1)–N(1a)
2.051(4)
Ni(1)–Br(1)
2.4975(8)
Ni(1)–N(2a)
2.057(4)
Ni(1)–Br(2)
2.5384(6)
Ni(1)–Br(1)
2.4014(8)
Ni(1)–O(1)
2.161(4)
N(2)–C(6)
1.273(6)
N(2)–C(6)
1.275(4)
N(2)–C(8)
1.437(6)
N(2)–C(8)
1.437(4)
Bond Angles (deg)
N(1)–Ni(1)–N(2)
78.98(15)
N(1)–Ni(1)–N(2)
78.58(11)
N(1a)–Ni(1)–N(2a)
78.56(15)
N(1)–Ni(1)–Br(1)
92.98(11)
N(1)–Ni(1)–Br(1)
95.46(10)
N(1)–Ni(1)–Br(2)
170.27(10)
N(1a)–Ni(1)–Br(1)
98.32(11)
N(2)–Ni(1)–Br(1)
100.72(9
N(2)–Ni(1)–Br(1)
119.82(10
N(2)–Ni(1)–Br(2)
92.98(7)
N(2a)–Ni(1)–Br(1)
132.52(10)
O(1)–Ni(1)–Br(1)
173.09(8)
N(1)–Ni(1)–N(2a)
92.84(14)
N(1)–Ni(1)–O(1)
87.25(14)
N(1a)–Ni(1)–N(2)
93.22(15)
N(2)–Ni(1)–O(1)
86.10(12)
N(1)–Ni(1)–N(1a)
166.18(15)
N(1)–Ni(1)–Br(2i)
95.19(9)
N(2)–Ni(1)–N(2a)
107.66(14)
N(2)–Ni(1)–Br(2i)
166.36(9)
ORTEP
diagram of bis-ligated Ni2(a) with thermal ellipsoids
shown at a probability level of 30%. All the hydrogen atoms have been
omitted for clarity.ORTEP diagram of 2Ni5·HO with thermal
ellipsoids shown at a probability level
of 30%. All the hydrogen atoms have been omitted for clarity.The molecular structure of 2Ni5·HO as shown in Figure revealed that the centrosymmetric
dimer
in which one bromide (Br(2) or Br(2))
per nickelcenter was bridged between the two nickelcenters while
the remaining bromides (Br(1) or Br(1)) occupied the apical position, similar structural observations
have been reported in the literature.[2d,4k,7a,7c,8a] In addition, each nickelcenter is bounded by two neutralchelating
nitrogen atoms of the ligand and a molecule ofwater per nickelcenter,
which acts as a monodentate ligand to Ni(1) or Ni(1), this led to a distorted octahedral geometry conformed to
the nickelcenter {O(1)–Ni(1)–Br(1) 173.09(8)°,
N(1)–Ni(1)–Br(2) 170.27(10)°, and N(2)–Ni(1)–Br(2) 166.36(9)°}.[4k−4m,12] The planes between the N(1), Ni(1), and N(2)chelating
rings and the aryl group are nearly perpendicular with a dihedral
angle of 87.01°, similar observations have been reported for
2-aryliminopyridylnickel analogs.[4d,7a,14] Besides, each nickelforms five-membered rings consisting
ofNi(1), N(1), C(5), and C(6), in which C(5) and C(6) deviate from
the coplane of atoms Ni(1), N(1), and N(2) with a distance of 0.082
or 0.144 Å, respectively. Ni(1) deviates at 0.152 Å from
the coplane consisting N(1), C(5), C(6), and N(2). There is no direct
bonding between the nickel atoms; however, the intermolecular distance
ofNi1···Ni1 was observed to be 3.544 Å.[4d,4k,9,11−14] Furthermore, the Ni(1)–N(1)pyridine bond length
(2.042(3) Å) is shorter than the Ni(1)–N(2)imine bond length (2.102(3) Å), indicating the better donor capability
of the pyridinenitrogen atoms.[4k−4m,5,8b,9,11,12]
Ethylene Polymerization
To identify the most suitable
co-catalyst for ethylenepolymerization, five different alkyl-aluminum
reagents such as EASC (ethylaluminum sesquichloride), Et2AlCl (diethylaluminum chloride), Me2AlCl (dimethylaluminumchloride), MAO (methylaluminoxane), and MMAO (modified methylaluminoxane)
were assessed with Ni1 selected as the test precatalyst.
A typicalpolymerization run as conducted under 10 atm ofC2H4 over 30 min in toluene (100 mL) at a temperature of
30 °C; and the results obtained are summarized in Table . Inspection of the results
shows that the catalytic performance of the co-catalysts decreased
in the following order as MAO > EASC > MMAO > Me2AlCl >
Et2AlCl. Therefore, considering the level of activity as
well as the different chemical nature of the aluminum activators,
MAO and EASC were selected for in-depth ethylenepolymerization reactions.
Table 2
Evaluation of Cocatalysts by Using
Precatalyst Ni1a
run
co-cat.
Al/Ni
T (°C)
t (min)
PE (g)
activityb
Mwc
Mw/Mnc
Tm (°C)d
1
EASC
400
30
30
6.38
6.38
6.93
2.3
77.9
2
Et2AlCl
400
30
30
4.93
4.93
6.92
2.3
85.7
3
Me2AlCl
400
30
30
5.84
5.84
5.19
2.1
71.4
4
MAO
2000
30
30
6.87
6.87
9.21
2.0
94.7
5
MMAO
2000
30
30
5.96
5.96
7.55
2.3
86.4
Conditions: 2.0 μmol Ni, 100 mL toluene, 10 atm
of C2H4,
30 min, and 30 °C.
106 g of PE (mol of Ni)−1 h–1.
Mw:
kg mol–1, determined by GPC.
Determined by DSC.
Conditions: 2.0 μmol Ni, 100 mL toluene, 10 atm
ofC2H4,
30 min, and 30 °C.106 g of PE (mol ofNi)−1 h–1.Mw:
kg mol–1, determined by GPC.Determined by DSC.
Ethylene Polymerization Using Ni1–Ni5/MAO
To establish an optimum ethylenepolymerization condition, precatalyst Ni1 was employed with MAO as a co-catalyst under 10 atm pressure
ofethylene. At a fixed temperature of 30 °C and a run time of
30 min, the Al/Ni ratio was gradually increased from 1500 to 3000
(runs 1–5, Table ). Inspection of the results shows that in a relatively low ratio
of 2500, the catalytic activity reached the maximum of 7.93 ×
106 g PE mol–1(Ni) h–1 (run 3, Table ).
Above 2500, the activity gradually decreased and at 3500 the lowest
activity of 5.08 × 106 g PE mol–1(Ni) h–1 was reached (run 5, Table ). The molecular weight of the obtained polyethylene
was increased in a similar way reaching 9.35 kg mol–1 with a molar ratio of 2500 (run 3, Table ) and then steadily decreased to 7.93 kg
mol–1 (run 5, Table ). This latter decrease in the molecular weight can
be ascribed to higher rates ofchain transfer as compared to chain
propagation at a higher molar ratio of the co-catalyst.[3b−3d,5,11,15] In addition, the molecular weight distribution
(Mw/Mn = 2.0–2.3)
remained narrow and unimodal as shown in the GPCcurves (Figure ).
Table 3
Optimization of the Polymerization
Conditions Using Ni1/MAOa
run
T (°C)
t (min)
Al/Ni
PE (g)
activityb
Mwc
Mw/Mnc
Tm (°C)d
1
30
30
1500
5.64
5.64
7.13
2.0
85.4
2
30
30
2000
6.87
6.87
9.21
2.0
94.7
3
30
30
2500
7.93
7.93
9.35
2.3
92.7
4
30
30
3000
6.81
6.81
8.59
2.3
89.7
5
30
30
3500
5.78
5.08
7.93
2.2
86.5
6
20
30
2500
4.48
4.48
15.19
2.4
104.8
7
40
30
2500
5.31
5.31
5.35
2.1
69.8
8
50
30
2500
2.06
2.06
4.30
2.0
62.6
9
30
05
2500
1.21
7.25
7.44
2.2
85.7
10
30
15
2500
3.76
7.52
7.89
2.3
96.1
11
30
45
2500
10.04
6.69
10.63
2.5
97.0
12
30
60
2500
11.15
5.58
12.43
2.5
101.0
13e
30
30
2500
2.80
2.80
5.73
2.2
68.8
14f
30
30
2500
trace
trace
Conditions: 2.0
μmol Ni1, 100 mL toluene, and 10 atm of C2H4.
106 g of PE (mol of Ni)−1 h–1.
Mw:
kg mol–1, determined by GPC.
Determined by DSC.
5 atm of C2H4.
1 atm of C2H4.
Figure 3
GPC curves of the obtained
polyethylene using Ni1/MAO
at different Al/Ni molar ratios (runs 1–5, Table ).
GPCcurves of the obtained
polyethylene using Ni1/MAO
at different Al/Ni molar ratios (runs 1–5, Table ).Conditions: 2.0
μmol Ni1, 100 mL toluene, and 10 atm ofC2H4.106 g of PE (mol ofNi)−1 h–1.Mw:
kg mol–1, determined by GPC.Determined by DSC.5 atm ofC2H4.1 atm ofC2H4.Using the fixed Al/Ni molar ratio
of 2500 with a reaction time
of 30 min, the temperature effect was studied from 20 to 50 °C
and the highest activity was achieved at 30 °C (runs 3, 6–8, Table ). Upon further increasing
the temperature, the catalytic activity rapidly decreased to 2.06
× 106 g PE mol–1(Ni) h–1 (run 8, Table )
at 50 °C, which can be attributed to the deactivation of active
species and lower solubility ofethylene at elevated temperature.[3b−3d,5,7c,8,9,11,14c] The molecular weight
of the obtained polymer decreased from 15.19 to 4.30 kg mol–1 (run 3, 6–8 Table ) as a function of elevation in temperature, suggesting a
higher chain termination rate compared to chain propagation at an
elevated reaction temperature.[3b−3d,5,7,15,16] Also, the molecular weight distribution remained
narrow (Mw/Mn = 2.0–2.4) and unimodal at various temperatures indicating
the single-site precatalyst, the corresponding GPCcurves are shown
in Figure .
Figure 4
GPC curves
of the obtained polyethylene using Ni1/MAO
at different reaction temperatures (runs 3, 6–8, Table ).
GPCcurves
of the obtained polyethylene using Ni1/MAO
at different reaction temperatures (runs 3, 6–8, Table ).The lifetime of the precatalyst was explored with the Al/Ni molar
ratio fixed at 2500 and temperature at 30 °C by conducting the
polymerization runs at 5, 15, 30, 45, and 60 min intervals using Ni1/MAO (runs 3, 9–12, Table ). We observed that the catalytic activity
was gradually increased in the first 30 min resulting in the maximum
activity of 7.93 × 106 g PE mol–1(Ni) h–1 (run 3, Table ). However, the activity slightly decreased
in the next 30 min, but still remains relatively high as 5.58 ×
106 g PE mol–1(Ni) h–1 even after 60 min (run 12, Table ); this highlights the longer lifetime of the active
species.[3c,3d,6,7a,14,15a,15b] The molecular weight of the
PE was gradually increased reaching a maximum of 12.43 kg mol–1 at 60 min. Significantly, all the run time of the
catalytic reaction and the molecular weight distribution remained
narrow (Mw/Mn = 2.2–2.5) and unimodal as shown in the GPCcurves (Figure ). The pressure ofethylenealso greatly affected the catalytic activity, as a much lower
activity at 5 atm and only a trace amount ofpolymer was observed
at 1 atm (runs 13 and 14, Table ). Additionally, the molecular weight of the obtained
polymer at 5 atm ofethylene was nearly half to that obtained with
10 atm, which can be attributed to a lower propagation rate at lower
ethylene pressure (runs 3 and 13, Table ).[3b−3d,4k,12]
Figure 5
GPC curves of the obtained polyethylene using Ni1/MAO
over different reaction times (runs 3, 9–12, Table ).
GPCcurves of the obtained polyethylene using Ni1/MAO
over different reaction times (runs 3, 9–12, Table ).Using the optimalconditions established for Ni1/MAO
(Al/Ni molar ratio = 2500, reaction temp. = 30 °C, and run time
= 30 min), the catalytic potential ofall the remaining precatalysts
(Ni2–Ni5) was evaluated toward ethylenepolymerization
with MAO (runs 1–5, Table ). The overall relative catalytic activities fell in
the following order, Ni1 > Ni2 > Ni3 > Ni4 > Ni5. Evidently,
the catalytic
activities were greatly influenced by the steric and electronic effects
of the N-aryl substituents. In terms of steric properties,
the least bulky precatalyst Ni1 displayed the highest
performance of 7.93 × 106 g PE mol–1(Ni) h–1 followed by Ni2 and Ni3. In terms of electronic effects, Ni4 and Ni5 displayed low activities because of the combination of
electron-withdrawing properties ofF or Cl and the steric effect of
the dibenzocycloheptyl group. The molecular weight of the obtained
polymer was significantly affected by the N-aryl
substituents with most sterically bulkier precatalyst Ni3 generating the highest molecular weight of up to 16.55 kg mol–1 followed by Ni2 with 12.19 kg mol–1 and dropped to 9.35 kg mol–1 with Ni1 (runs 1–3 Table ). The lower molecular weight polymers (2.22–5.81
kg mol–1) were observed with ortho-halidecounterpart precatalysts. Besides, the molecular weight distribution
remained narrow (Mw/Mn = 2.1–2.4) and unimodal; suggesting a single-site
active center as shown in the GPCcurves (Figure ). In contrast, the melting temperature (Tm) ofpolyethylene displayed by the precatalysts
bearing ortho-halideNi4 or Ni5 (Tm = 106.8 or 109.0 °C) is higher
than that generated by the precatalysts bearing alkyl counterparts
as for Ni1–Ni3 (Tm = 89.1–96.1 °C). These observations suggest that electron-withdrawing
ortho-substituents (Cl or F) suppressed “chain walking”
and favored β-H elimination. It is uncertain to explain this
finding but it might be because of weak hydrogen bonding or dipole
interaction ofortho-fluorine or chlorine with coordinated
ethylene during the insertion
transition state; these findings are consistent with the literature.[4k,12,17]
Table 4
Ethylene
Polymerization by Using Ni1–Ni5/MAO
under Optimized Conditionsa
run
precat.
mass of PE (g)
activityb
Mwc
Mw/Mnc
Tm (°C)d
1
Ni1
7.93
7.93
9.35
2.3
92.7
2
Ni2
5.62
5.62
12.19
2.4
96.1
3
Ni3
2.53
2.53
16.55
2.3
89.1
4
Ni4
2.24
2.24
5.81
2.4
106.8
5
Ni5
2.12
2.12
2.22
2.1
109.0
Conditions: 2.0 μmol Ni, 100 mL toluene,
10 atm of C2H4,
30 min, 30 °C, and the Al/Ni ratio of 2500.
106 g of PE (mol of Ni)−1 h–1.
Mw:
kg mol–1,determined by GPC.
Determined by DSC.
Figure 6
GPC curves of the obtained polyethylene
using Ni1–Ni5/MAO under optimized
conditions (runs 1–5, Table ).
GPCcurves of the obtained polyethylene
using Ni1–Ni5/MAO under optimized
conditions (runs 1–5, Table ).Conditions: 2.0 μmol Ni, 100 mL toluene,
10 atm ofC2H4,
30 min, 30 °C, and the Al/Ni ratio of 2500.106 g of PE (mol ofNi)−1 h–1.Mw:
kg mol–1,determined by GPC.Determined by DSC.
Ethylene Polymerization Using Ni1–Ni5/EASC
With EASC as the co-catalyst, a parallel investigation was performed
as that described for the MAO system. Once again Ni1 was
selected as the test precatalyst for optimization ofpolymerization
parameters; the results are summarized in Table . Upon varying the Al/Ni molar ratio from
300 to 700, the highest catalytic performance of 6.75 × 106 g PE mol–1(Ni) h–1 was
observed at a ratio of 500 at 30 °C (runs, 1–5, Table ). While the highest
molecular weight ofpolyethylene was 7.27 kg mol–1 achieved using an Al/Ni ratio of 400 and then gradually decreased
to 6.66 kg mol–1, this reduction in the molecular
weight can be attributed to a higher chain transfer rate versus chain
propagation rate at a higher molar ratio of the co-catalyst;[3b−3d,5,11,15] the corresponding GPCcurves are shown in Supporting Information (S2, Figure S1). The molecular
weight distribution remained in the narrow range (Mw/Mn = 2.0–2.3) and
was unimodal; suggesting a single-site active species, displaying
the same results as those obtained with the Ni1/MAO system.
Table 5
Optimization of the Polymerization
Conditions Using Ni1/EASCa
run
T (°C)
t (min)
Al/Ni
mass of PE (g)
activityb
Mwc
Mw/Mnc
Tm (°C)d
1
30
30
300
2.14
2.14
6.93
2.3
77.9
2
30
30
400
6.38
6.38
7.27
2.0
84.8
3
30
30
500
6.75
6.75
6.81
2.0
87.4
4
30
30
600
5.82
5.82
6.75
2.0
84.1
5
30
30
700
5.03
5.03
6.66
2.0
83.9
6
20
30
500
5.04
5.04
12.67
2.3
101.1
7
40
30
500
4.50
4.50
5.01
2.0
70.3
8
50
30
500
1.97
1.97
3.96
1.8
64.0
9
30
05
500
1.03
6.18
6.00
2.0
88.8
10
30
15
500
3.16
6.32
6.26
2.0
81.9
11
30
45
500
7.93
5.29
7.58
2.2
85.1
12
30
60
500
9.31
4.66
7.81
2.1
87.1
13e
30
30
500
2.34
2.34
4.77
1.8
65.3
14f
30
30
500
trace
trace
Conditions: 2.0
μmol Ni1, 100 mL toluene, and 10 atm of C2H4.
106 g of PE (mol of Ni)−1 h–1.
Mw:
kg mol–1, determined by GPC.
Determined by DSC.
5 atm of C2H4.
1 atm of C2H4.
Conditions: 2.0
μmol Ni1, 100 mL toluene, and 10 atm ofC2H4.106 g of PE (mol ofNi)−1 h–1.Mw:
kg mol–1, determined by GPC.Determined by DSC.5 atm ofC2H4.1 atm ofC2H4.Monitoring the activity ofNi1/EASC, the temperature
was varied from 20 to 50 °C (runs 3, 6–9), again exhibiting
similar trends to that of the Ni1/MAO system and the
peak performance of 6.75 × 106 g PE mol–1(Ni) h–1 was observed at 30 °C (run 3, Table ). Furthermore, upon
increasing the temperature, a dramatic drop in the activity (1.97
× 106 g PE mol–1(Ni) h–1) was observed at 50 °C (run 8, Table ). This decrease in the activity at elevated
temperature can be attributed to the lower solubility ofethylene
and the deactivation of the active species. Furthermore, a decrease
trend from 12.67 to 3.96 kg mol–1 was observed in
the molecular weight of the obtained polyethylene (run 3, 6–8 Table ) as a result of increasing
the temperature, suggesting a higher chain termination rate versus
chain propagation rate at elevated temperature;[3b−3d,7,15,16] the temperature effects on the molecular weight of the obtained
polyethylene are further shown in the GPCcurves (Supporting Information S2, Figure S2). Additionally, the molecular
weight distribution remained in the narrow range (Mw/Mn = 1.8–2.3) and
unimodal at various reaction temperatures.With a fixed Al/Ni
molar ratio of 500 and a reaction temperature
of 30 °C, polymerization runs were performed between intervals
of 5 and 60 min (runs 3, 9–12, Table ). The activity was gradually increased reaching
its peak performance of 6.75 × 106 g PE mol–1(Ni) h–1 (run 3, Table ) at 30 min and then progressively dropped
over longer time with the lowest value of 4.66 × 106 g PE mol–1(Ni) h–1 at 60 min
(run 12, Table ).
The molecular weight of the obtained polyethylene steadily increased
as the time was prolonged reaching 7.81 kg mol–1 at 60 min, nevertheless lower than that obtained using the Ni1/MAO system; further illustrated in the GPCcurves (Supporting Information S2, Figure S3). Moreover,
the unimodal molecular weight distribution in the narrow range (2.0–2.2)
was the characteristicfeature of the obtained polyethylene. Furthermore,
similar observations are made for the effect of pressure on the activity
and molecular weight to those observed with Ni1/MAO.Under the optimized conditions determined for Ni1/EASC
such as the Al/Ni molar ratio = 500, reaction temperature = 30 °C,
and run time = 30 min, all the remaining nickel precatalysts Ni2–Ni5 were also screened and the results are shown
in Table . The activities
followed a similar decreasing order to those observed earlier with
the MAO-activated precatalysts. Moreover, these EASC-activated precatalysts
displayed slightly lower activities than those ofNi1–Ni5/MAO indicating the importance of the alkyl-aluminoxane activator.
Almost similar steric and electronic effects can be used for explanation
of activities with least steric precatalyst Ni1 again
exhibiting the highest activity of 6.75 × 106 g PE
mol–1(Ni) h–1, while the highest
molecular weight of 14.42 kg mol–1 ofpolyethylene
was achieved with the bulkier precatalyst Ni3 (runs 1
and 3, Table ). Interestingly,
similar trends for the molecular weight were observed to those obtained
with Ni/MAO system. Moreover, the molecular weight distribution
was in the narrow range (Mw/Mn = 1.6–2.2) and was unimodal; suggesting again
that the current precatalyst generates a single-site active species
as shown in the GPCcurves (Supporting Information S2, Figure S4). The melting temperatures (Tm) of the obtained polyethylene again show similar trends
to those observed with the Ni/MAO system; similar observations
have been reported in the literature.[4k,4l,12,17]
Table 6
Ethylene Polymerization Using Ni1–Ni5/EASC under
Optimized Conditionsa
run
precat.
mass of PE (g)
activityb
Mwc
Mw/Mnc
Tm (°C)d
1
Ni1
6.75
6.75
6.81
2.0
87.4
2
Ni2
4.58
4.58
9.76
2.2
85.4
3
Ni3
2.07
2.07
14.42
2.1
83.3
4
Ni4
2.13
2.13
4.01
2.1
99.8
5
Ni5
2.01
2.01
1.41
1.6
101.3
Conditions: 2.0 μmol Ni, 100 mL toluene,
10 atm of C2H4,
30 min, 30 °C, and the Al/Ni ratio of 500.
106 g of PE (mol of Ni)−1 h–1.
Mw:
kg mol–1,determined by GPC.
Determined by DSC.
Conditions: 2.0 μmol Ni, 100 mL toluene,
10 atm ofC2H4,
30 min, 30 °C, and the Al/Ni ratio of 500.106 g of PE (mol ofNi)−1 h–1.Mw:
kg mol–1,determined by GPC.Determined by DSC.
Microstructural Studies of Polyethylenes
The melting
point (Tm) of the obtained polymers using Ni1–Ni5 with either MAO or EASCfell in the range 83.3–109.0
°C with a slight difference seen between the cocatalysts (89.1–109.0
°C with MAO versus 83.3–101.3 °C with EASC) as shown
in Tables and 6, respectively. This range of melting points would
suggest the branching in the polyethylenes. To study the influence
of steric/electronic variations in the ligand framework as well as
the cocatalyst and temperature effect on the microstructure ofpolyethylene,
high-temperature 1H and 13CNMR spectroscopy
was conducted for representative samples ofpolyethylene. The NMR
spectral data of the obtained samples using Ni4/MAO and Ni5 bearing an electron-withdrawing ortho-substituent (Cl
or F) were compared to the data obtained using Ni1–Ni3/MAO with an ortho-alkyl group (Me, Et, or i-Pr). All the calculations for the data and peak assignments
were performed according to the literature reports;[18] the NMR data and the calculations of the branching levels
for the selected polyethylene samples are provided in Supporting Information S3.In general,
the 1HNMR spectra of the obtained polyethylenes using Ni1–Ni5 with MAO (runs 1–5, Table ) disclose the existence ofvinyl and vinylenefunctional groups with characteristics signals
at δ 5.91 (Hb) and 5.06 (Ha) with an integration
ratio of 1:2 (−CH=CH2) and a signal at δ
5.50 (Hc/Hc′) for the −CH=CH–
functional group. Inspection of the spectral results reveals that
the vinylene to a vinyl ratio ((−CH=CH−)/(−CH=CH2)) was notably affected by the ortho-substituents in the precatalysts
and was in the range of 6.9:1 to 1.8:1 (Figure ) and also see Supporting Information S4, Figure S5. The vinyl end group as a function
of precatalysts followed the order as Ni5 ≈ Ni4 > Ni1 > Ni2 > Ni3, suggesting
that the electron-withdrawing fluorine or chlorine group at the ortho-position
favored generating a polymer with vinyl end groups.
Figure 7
1H NMR spectra
of the obtained polyethylene samples
with Ni1, Ni2, and Ni5 at 30
°C using MAO (runs 1, 2, 5, Table ); recorded at 100 °C in d-C2D2Cl4.
1HNMR spectra
of the obtained polyethylene samples
with Ni1, Ni2, and Ni5 at 30
°C using MAO (runs 1, 2, 5, Table ); recorded at 100 °C in d-C2D2Cl4.This vinylene/vinylene unsaturation was further explained using
the 13CNMR spectrum of the polyethylene samples obtained
using Ni1/MAO (run 1, Table ), indicating the characteristics peaks for
the corresponding alkene-carbon atoms such as Ca, Cb, Cc, and Cc′ (Figure ). Analysis of the sample spectrum
reveals highly branched contents (68 branches/1000 Cs) including methyl
(73.6%), ethyl (2.2%), propyl (1.4%), butyl (3.9%), amyl (1.9%), 1,4-paired
methyl (4.6%), 1,6-paired methyl (3.7%), and longer-chain branches
(8.7%). Almost similar observations were made for the obtained sample
ofpolyethylene using Ni2/MAO (run 2, Table ), which displayed almost similar
types of branching with the corresponding peaks for vinylene and vinyl
groups along with upfield saturated peaks and showed total branches
of 69/1000 Cs (Supporting Information S4, Figure S6).
Figure 8
13C NMR spectrum of the obtained polyethylene
sample
with Ni1/MAO at 30 °C (run 1, Table ); recorded at 100 °C in d-C2D2Cl4.
13CNMR spectrum of the obtained polyethylene
sample
with Ni1/MAO at 30 °C (run 1, Table ); recorded at 100 °C in d-C2D2Cl4.In stark contrast, the 13CNMR spectrum of the obtained
polyethylene using Ni5/MAO (run 5, Table ) displayed much lower branches of 17/1000
Cs (Figure ), consisting
of methyl (58.4%), butyl (6.1%), 1,4-paired methyl (3.2%), and longer-chain
branches (32.3%). Moreover, the signal intensity of the vinyl end
groups (Ca and Cb) is higher than that seen
for the vinylene group (Hc or Hc′), which
is in accordance with the corresponding 1HNMR data (vinylene
to vinyl ratio = 1.8:1). These observations suggest that substitution
offluorine at the ortho-position favored β-H elimination and
reduced “chain walking”. It is uncertain to explain
this finding but it might be because of weak hydrogen bonding between
the coordinated ethylene and ortho-fluorine during
the insertion transition state. This lower branching level was also
supported by the high melt temperature (Tm) of the corresponding polyethylene sample; similar findings have
been found in the literature.[2d,8a,12,17c,17d,18]
Figure 9
13C NMR spectrum of the obtained
polyethylene sample
with Ni5/MAO at 30 °C (run 5, Table ); recorded at 100 °C in d-C2D2Cl4.
13CNMR spectrum of the obtained
polyethylene sample
with Ni5/MAO at 30 °C (run 5, Table ); recorded at 100 °C in d-C2D2Cl4.Additionally, the high-temperature 13CNMR spectrum
ofpolyethylene samples obtained with Ni4/MAO (run 4, Table ) was recorded and
also showed lower branches of 34/1000 Cs (Supporting Information S4, Figure S7). The explanation for this lower
degree of branching is again ambiguous but may be because of the high
electronegative nature ofchlorine, which may interact with the coordinated
ethylene that suppresses chain-walking and favors β-H elimination.
Furthermore, the temperature greatly influences the catalytic performance
and its effect was investigated on the microstructure of the polyethylene
generated by Ni1/MAO at 30, 40, and 50 °C (runs
3, 7, 8, Table ).
The 1HNMR spectra displayed that upon increasing the temperature
from 30 to 50 °C, the vinylene/vinyl ratio increases from 5.81:1
to 9.82:1 (Figure ); suggesting that higher temperature had increased the rate of termination
and hence within the polymerchain increased the vinylene portions.
Figure 10
1H NMR spectra of the obtained polyethylene samples
with Ni1/MAO at 30, 40, and 50 °C (runs 3, 7, 8, Table ); recorded at 100
°C in d-C2D2Cl4.
1HNMR spectra of the obtained polyethylene samples
with Ni1/MAO at 30, 40, and 50 °C (runs 3, 7, 8, Table ); recorded at 100
°C in d-C2D2Cl4.In contrast to 30 °C, the 13CNMR spectrum of a
sample obtained at 50 °C (run 8, Table ) showed a higher number of branches of 121/1000
Cs (Supporting Information S4, Figure S8);
suggesting that higher temperature increases β-H elimination.
Additionally, the effect of the co-catalyst on the microstructure
ofpolyethylene was studied and the 1H and 13CNMR spectra of the obtained samples using Ni1 (run
1, Table ) and Ni5 (run 5, Table ) with EASC were recorded. Similar variations in the melting
points were seen to those observed using Ni/MAO, which
suggests similar effects on the microstructure. Likewise, again both
types of the unsaturated peaks were observed with a downfield chemical
shift in the 1HNMR spectra with the vinylene/vinyl ratio
decreasing from 7.6:1 to 2.5:1, which can be attributed to the fact
that the electron-withdrawing substituent (fluorine) at the ortho-position
compared to the ortho-alkyl substituent favored to
produce polyethylene ofvinyl end groups (Figure ).
Figure 11
1H NMR spectra of the obtained polyethylene
samples
with Ni1 and Ni5 using EASC at 30 °C
(runs 1 and 5, Table ); recorded at 100 °C in d-C2D2Cl4.
1HNMR spectra of the obtained polyethylene
samples
with Ni1 and Ni5 using EASC at 30 °C
(runs 1 and 5, Table ); recorded at 100 °C in d-C2D2Cl4.These vinylene/vinyl
units were also confirmed by the 13CNMR spectrum obtained
using EASC/Ni1 (run 1, Table ), which showed high
branches of 83 per 1000 Cs (Supporting Information S4, Figure S9); including methyl (69.8%), ethyl (5.4%), propyl
(1.8%), butyl (3.1%), amyl (1.8%), 1,4-paired methyl (4.2%), 1.6-paired
methyl (2.7%), and longer-chain branches (11.2%). In addition, much
contrast results of the 13CNMR spectrum of the resulting
polyethylene using Ni5/EASC were obtained (run 5, Table ), again displaying
much lower branches of 16/1000 Cs; mainly comprising methyl (54.6%),
butyl (4.2%), amyl (7.1%), 1,4-paired methyl (1.9%), 1,6-paired methyl
(3.4%), and longer-chain branches (28.8%) (Figure ). These lower-branching contents suggest
that electron-withdrawing fluorine at the ortho-position reduced “chain
walking” and preferred β-H elimination.[2d,8a,12,17a,17d,18,19] Furthermore, these findings also suggest
that the co-catalysts (MAO and EASC) have a slight impact on the microstructure
for the desired unsaturated (vinyl/vinylene double bonds) branched
polyethylene.
Figure 12
13C NMR spectrum of the obtained polyethylene
sample
with Ni5/EASC at 30 °C (run 5, Table ); recorded at 100 °C in d-C2D2Cl4.
13CNMR spectrum of the obtained polyethylene
sample
with Ni5/EASC at 30 °C (run 5, Table ); recorded at 100 °C in d-C2D2Cl4.
Comparison between the Reported and Current Precatalysts
To explore the overall influence of the 2,4-bis(dibenzocycloheptyl)
groups along with the variations in the steric and electronic properties
of the ortho-substituent, the catalytic performance, molecular weight,
and dispersity of the current nickel precatalyst system (G) are compared with those of the previously reported systems D, E, and F under optimized conditions
at 10 atm ofethylene (Figure ).[4k,11] In terms of activity, the precatalyst D (13.8 × 106 g PE mol–1(Ni) h–1) was proved to be the most active followed
by the current system G. The relative catalytic activities
were found to be in the order D > G > E > F. However, the molecular weight of the
obtained
polyethylene with current system G is the second highest
with a narrow dispersity (Mw/Mn = 2.4), which is comparable to those obtained with D and E; and much narrow than that observed with F. It shows that the catalytic performance of the current
system bears some resemblance to those of D, E, and F. More significantly, the current catalytic system
has the propensity of generating highly branched unsaturated (vinyl/vinylene)
polyethylene with a major class of the internal double bond (vinylene).
Figure 13
Comparison
of the previously reported systems bearing N-2,4-bis(dibenzhydryl)
or N-2,4-bis(fluorenyl) and
the current system with N-2,4-bis(dibenzocycloheptyl)
groups under optimal conditions at 10 atm of C2H4 (D–G).
Comparison
of the previously reported systems bearing N-2,4-bis(dibenzhydryl)
or N-2,4-bis(fluorenyl) and
the current system with N-2,4-bis(dibenzocycloheptyl)
groups under optimalconditions at 10 atm ofC2H4 (D–G).
Conclusions
In summary, we have successfully synthesized
a series of2-(2,4-dibenzocycloheptyl-6-R-phenylimino)ethyl)pyridine,
R = Me (L1), Et (L2), i-Pr (L3), Cl (L4), or F (L5)) and the corresponding nickel(II) bromidecomplexes (Ni1–Ni5) in good yield. All the organiccompounds and the precatalysts were
stable in the air and were characterized by FT-IR, 1H,
and 13CNMR spectroscopy as well as by elemental analysis.
The molecular structures ofcomplexes Ni2 and Ni5 were the subject for the single-crystal X-ray diffraction analysis.
The structure ofcomplex Ni2can be best described as
a distorted-square pyramidal and Ni5 with a bromide bridged
dimericform revealed distorted-octahedral geometry. When activated
with either MAO or EASC, all the precatalysts displayed high activity
in the range of 2.12 to 7.93 × 106 g of PE (mol ofNi)−1 h–1 (MAO) and 2.01 to 6.75
× 106 g of PE (mol ofNi)−1 h–1 (EASC) producing highly branched polyethylene of
low-molecular-weights in the range of 1.41–16.55 kg/mol with
unsaturated end groups and with the internal double bond as the major
class (vinylene/vinyl = 9.8:1 to 1.8:1). The catalytic activity, the
type of unsaturation, and branching contents are greatly influenced
by the nature of the ortho-substituent and temperature. Significantly,
the precatalysts Ni4 and Ni5 (R = Cl or
F) displayed lower catalytic activities and the obtained polyethylene
showed high melting temperature with the least number of branches
as compared to that with Ni–Ni3 (R = Me, Et, or i-Pr); these observations were also consistent with the
high-temperature 1H and 13CNMR spectral analyses.
Experimental
Section
General Considerations
All the moisture and/or air-sensitive
compounds were handled under an inert nitrogen atmosphere using standard
Schlenk techniques. All the solvents were heated to reflux prior to
use, distilled, and used under the nitrogen atmosphere. The cocatalysts
such as MAO (methylaluminoxane, 1.46 M in toluene) and MMAO (modified
methylaluminoxane, 1.93 M in heptane) were purchased from Akzo Nobel
Corp; whereas Et2AlCl (diethylaluminum chloride, 0.79 M
in toluene) and (EASC (Et3Al2Cl3,
0.87 M in toluene)) were purchased from Acros Chemicals. Ethylene
of high purity was purchased from Beijing Yanshan PetrochemicalCo.,
used as received, and all other reagents were purchased from Aldrich,
Acros, or local suppliers. The corresponding anilines (2,4-bis(dibenzocycloheptyl)-R-phenylamine,
R = Me, Et, i-Pr, Cl, or F) were prepared according
to the procedure reported in the literature.[3b,4i,12,20] The NMR spectra
were recorded on a Bruker DMX (400 MHz instrument) at ambient temperature
using TMS as an internal standard. A PerkinElmer System 2000 FT-IR
spectrometer was used for the analysis ofFT-IR spectra and a Flash
EA 1112 microanalyzer was used for elemental analysis. Molecular weight
(Mw) and molecular weight distribution
(Mw/Mn) of
the obtained polyethylene were determined by PL-GPC220 at 150 °C
using 1,2,4-trichlorobenzene as a solvent. The melting temperatures
were determined by using differential scanning calorimetry (DSC, TA2000)
under a nitrogen atmosphere. A typicalpolyethylene sample in the
range of 4.5–5.5 mg was heated up to 130 °C at a heating
rate of 20 °C per min for 5 min at the same temperature to remove
its thermal history and then cooled to −50 °C at the same
heating rate. For recording high-temperature 1H and 13CNMR spectra, a weighed amount ofpolyethylene (90–100
mg) in 1,1,2,2-tetrachloroethane-d2 (2
mL) was used with TMS as an internal standard. Inverse gated 13C spectra were recorded on a Bruker DMX 300 spectrometer
at 75.47 MHz in 5 mm standard glass tubes at 100 °C with the
number of scans between 3642 and 4982. The operationalconditions:
spectral width 1882.4 kHz; acquisition time 0.870–1.8 s; relaxation
delay 2.0 s, and with a pulse width of 15.5 μs. The branching
contents were calculated from the integration of the corresponding
peaks in the 13CNMR spectra according to the literature.[18] The procedure for the synthesis of a series
of sterically and electronically modified bulky anilines are given
in the Supporting Information.
Synthesis of
Ligands (L1–L5)
2-{N-2,4-(C15H13)-6-MeC6H2}C7H7N (L1)
A mixture of2-actylpyridine
(0.25 g, 2.07 mmol) and 2,4-bis(dibenzocycloheptyl)-6-methylaniline
(1.01 g, 2.07 mmol) in toluene (50 mL) was refluxed for 20 min using
Dean–Stark trap, followed by the slow addition ofp-toluenesulfonic acid (cat. 15 mol %) and the reaction mixture was
further refluxed for 8 h. Upon cooling to room temperature, all the
volatiles were removed under reduced pressure and the residue was
purified through alumina (basic) column chromatography using petroleum
ether/ethyl acetate (25:2) as an eluent to offer L1 as
a yellow powder (0.78 g 63%). mp 130–132 °C. FT-IR (cm–1): 3055 (w), 3014 (w), 2925 (w), 2871 (w), 2831 (w),
1644 (ν(C=N), m), 1588 (w), 1566 (w), 1491 (m), 1465
(m), 1434 (m), 1362 (m), 1302 (w), 1241 (w), 1215 (w), 1163 (w), 1133
(w), 1103 (m), 1044 (w), 1024 (w), 993 (w), 967 (w), 942 (w), 917
(w), 882 (w), 842 (w), 808 (w), 754 (s), 707 (m), 677 (w). 1HNMR (400 MHz, CDCl3, TMS): δ 8.64 (d, J = 4.80 Hz, 1H, Py-H), 8.40 (d, J = 8.00
Hz, 1H, Py-H), 7.83 (t, J = 7.80 Hz, 1H, Py-H), 7.40–7.37
(m, 1H, Py-H), 7.20–6.82 (m, 15H, Ar-H), 6.59 (s, 1H, Ar-Hm), 6.51 (t, J = 7.40 Hz, 1H, Ar-H), 6.42
(s, 1H, Ar-Hm), 5.09 (s, 1H, −CH−), 4.96
(s, 1H, −CH−), 3.12–2.89 (m, 3H, −CH2−), 2.75–2.55 (m, 4H, −CH2−), 2.32–2.26 (m, 1H, −CH2−),
1.79 (s, 3H, −CH3), 1.41 (s, 3H, −CH3). 13CNMR (100 MHz, CDCl3, TMS): δ
168.9, 156.0, 148.4, 145.7, 141.4, 141.2, 140.2, 140.0, 139.7, 139.6,
139.3, 138.6, 138.4, 136.1, 131.5, 131.4, 131.2, 131.1, 131.0, 130.9,
130.5, 130.2, 129.3, 128.6, 127.1, 127.0, 126.8, 126.6, 126.4, 126.0,
125.9, 125.6, 125.4, 124.7, 124.6, 121.4, 57.8, 56.4, 32.6, 32.5,
31.9, 30.4, 17.9, 16.1. Anal. calcd for C44H38N2 (594.80): C, 88.85; H, 6.44; N, 4.71. Found: C, 88.47;
H, 6.84; N, 4.59.
Under the nitrogen
atmosphere, 2-(2,4-bis(dibenzocycloheptyl)-6-methylphenyl)iminoethyl)pyridine
(0.31 g, 0.52 mmol) and NiBr2(DME) (0.08 g, 0.26 mmol)
were loaded into dichloromethane (10 mL) and ethanol (10 mL) and stirred
for 14 h at room temperature. After which, all the volatiles were
evaporated under reduced pressure, followed by the addition of diethyl
ether into the residue to induce precipitation. The precipitate was
filtered, washed with an excess ofdiethyl ether (3 × 10 mL),
and dried to afford Ni1 as a green powder (0.40 g, 95%).
FT-IR (cm–1): 3058 (w), 3016 (w), 2931 (w), 2884
(w), 2832 (w), 1624 (ν(C=N), m), 1595 (m), 1572 (w),
1492 (m), 1438 (m), 1370 (m), 1319 (m), 1259 (w), 1210 (w), 1162 (w),
1102 (w), 1050 (w), 1023 (w), 986 (w), 945 (w), 880 (w), 837 (w),
765 (s), 704 (m), 676 (m). Anal. calcd for C44H38Br2N2Ni·2H2O (849.33): C, 62.22;
H, 4.98; N, 3.30. Found: C, 62.18; H, 4.86; N, 3.25.
[2-{N-2,4-(C15H13)-6-EtC6H2}C7H7N]NiBr2 (Ni2)
Using a similar procedure and molar
ratios to those described for the synthesis ofNi1, Ni2 was isolated as a green powder (0.41 g, 95%). FT-IR (cm–1): 3059 (w), 3016 (w), 2970 (w), 2933 (w), 2877 (w),
2833 (w), 1623 (ν(C=N), m), 1595 (m), 1571 (w), 1492
(m), 1447 (m), 1370 (m), 1317 (m), 1259 (w), 1206 (w), 1161 (w), 1102
(w), 1052 (w), 1022 (w), 982 (w), 946 (w), 880 (w), 877 (w), 833 (w),
764 (s), 704 (m), 676 (m). Anal. calcd for C45H40Br2N2Ni·2H2O (863.36): C, 62.60;
H, 5.14; N, 3.24. Found: C, 62.86; H, 4.95; N, 3.22.
[2-{N-2,4-(C15H13)-6-i-PrC6H2}C7H7N]NiBr2 (Ni3)
Using a similar procedure
and molar ratios to those described for the synthesis ofNi1, Ni3 was isolated as a green powder (0.36 g, 82%).
FT-IR (cm–1): 3058 (w), 3014 (w), 2965 (w), 2932
(w), 2875 (w), 2830 (w), 1621 (ν(C=N), w), 1595 (m), 1571 (w),
1493 (m), 1445 (m), 1371 (m), 1317 (m), 1259 (w), 1204 (w), 1163 (w),
1136 (w), 1103 (w), 1051 (w), 1025 (w), 982 (w), 947 (w), 877 (w),
830 (w), 766 (s), 704 (m), 678 (m). Anal. calcd for C46H42Br2N2Ni·H2O (859.37):
C, 64.29; H, 5.16; N, 3.26. Found: C, 64.30; H, 5.12; N, 3.25.
[2-{N-2,4-(C15H13)-6-ClC6H2}C7H7N]NiBr2 (Ni4)
Using a similar procedure and molar
ratios to those described for the synthesis ofNi1, Ni4 was isolated as a green powder (0.40 g, 93%). FT-IR (cm–1): 3059 (w), 3013 (w), 2933 (w), 2878 (w), 2831 (w),
1627 (ν(C=N), m), 1595 (m), 1595 (w), 1571 (w), 1492
(m), 1447 (m), 1405 (w), 1369 (m), 1318 (m), 1259 (w), 1220 (w), 1162
(w), 1132 (w), 1101 (w), 1051 (w), 1022 (w), 983 (w), 948 (w), 878
(w), 827 (w), 765 (s), 695 (m), 673 (m), 652 (m). Anal. calcd for
C43H35Br2ClN2Ni·H2O (851.73): C, 60.64; H, 4.38; N, 3.29. Found: C, 60.67; H,
4.30; N, 3.22.
[2-{N-2,4-(C15H13)-6-FC6H2}C7H7N]NiBr2 (Ni5)
Using a similar
procedure and molar
ratios to those described for the synthesis ofNi1, Ni5 was isolated as a green powder (0.39 g, 95%). FT-IR (cm–1): 3060 (w), 3014 (w), 2933 (w), 2876 (w), 2832 (w),
1627 (ν(C=N), m), 1597 (m), 1570 (w), 1490 (m), 1448
(w), 1423 (m), 1370 (m), 1320 (w), 1282 (w), 1260 (w), 1204 (w), 11621
(w), 1133 (w), 1104 (w), 1050 (w), 1023 (w), 995 (w), 945 (w), 915
(w), 875 (w), 830 (w), 766 (s), 738 (s), 704 (m), 675 (m). Anal. calcd
for C43H35Br2FN2Ni·H2O (835.28): C, 61.83; H, 4.47; N, 3.35. Found: C, 61.71; H,
4.41; N, 3.34.
Typical Procedure for Ethylene Polymerization
High
pressure (10 atm) ethylenepolymerization was conducted in a 250 mL
stainless steel autoclave, equipped with pressure and temperature
control systems and a mechanical stirrer. The autoclave was evacuated
and back-filled three times with nitrogen and once with ethylene.
The precatalyst (2.0 μmol) was dissolved in toluene (25 mL)
and when the required temperature was reached, the complex solution
was injected into the autoclave containing ethylene (ca. 1 atm) followed
by the addition of more toluene (25 mL). The required amounts ofco-catalyst
(Me2AlCl, Et2AlCl, EASC, MAO, or MMAO), followed
by the addition oftoluene (50 mL), were successively added using
a syringe making the total volume to 100 mL. The autoclave was immediately
pressurized to the predetermined ethylene pressure and stirred (400
rpm). After reaching the required reaction time, the reactor was cooled
in a water bath and stopped the flow ofethylene and then slowly released
the ethylene pressure. The reaction was quenched with 10% hydrochloric
acid solution in ethanol. The polymer was collected, filtered, washed
with ethanol, and dried under reduced pressure at 40 °C and then
weighed. Using a similar procedure to that described for 10 atm ofethylene, 5 atm ethylenepolymerization was also conducted. While
the Schlenk tube was used instead of an autoclave for 1 atm ethylenepolymerization.
X-ray Crystallographic Studies
X-ray
diffraction studies
were conducted for the suitable single-crystal ofNi2 and Ni5. Crystals were grown by the layering ofheptane
into the solution of the corresponding complex in dichloromethane
at ambient temperature. The X-ray structural determination was carried
out on a Rigaku Saturn 724+ CCD diffractometer provided with graphite
monochromatic Mo Kα radiation (λ = 0.71073 Å) at
173(2) K. The cell parameters were obtained by a global refinement
of the positions ofall the collected reflections. The intensities
for Lorentz and polarization effects were corrected out and an empirical
absorption was applied. The structures were resolved by the direct
methods and refined by full-matrix least-squares on F2. All hydrogen atoms were placed in the calculated positions.
Structure solution and refinement were conducted by using SHELXT-97.[21] The free solvent molecules were squeezed with
PLATON software.[22] The details of the X-ray
structure determination data and structural refinements for Ni2 and Ni5 are provided in Table .
Table 7
Crystal
Data and Structure Refinement
for Ni2(a) and 2Ni5·HO
Authors: Igor E Soshnikov; Konstantin P Bryliakov; Artem A Antonov; Wen-Hua Sun; Evgenii P Talsi Journal: Dalton Trans Date: 2019-05-09 Impact factor: 4.390