K. Wang et al.
MolecularCatalysis465(2019)43–53
molar ratio of benzylalcohol and benzylamine, is represented as A and
B, respectively. It is obviously seen that the optimized molar ratio is SA
:
SB = 5 : 4 in the N-alkylated reaction. The optimum reaction conditions
of the hydrogenation of nitroarenes reaction were confirmed to be that
the temperature is 90 °C and the dosage of hydrazine is 15 mmol, and
more detailed explanations of screening the reaction conditions are
shown in Fig. S.5.
To study the generalities of the catalyst, other types of aromatic
alcohol, amines and nitroarenes were chosen for N-alkylated reaction
and nitroarenes reduction under the optimal reaction condition, re-
spectively. Different type substrates are converted to relevant products
with well conversion and selectivity in Tables 3–5. It can be clearly seen
from Table 3, the yield of N- alkylation reaction by various aromatic
alcohols and aniline was more than 85% under the optimum reaction
conditions, whether the substituent of alcohols is an electron-absorbing
group or an electron-supplying group. As for Table 4, entries 1–10 and
13–15, imines are produced via benzylalcohol together with different
derivatives of arylamines. Besides entries 7, 8 and 15, the yields of these
reactions are all over 75%. Especially for entries 11 and 12, the re-
actants of amines are fatty amines, these yields are at least 85%.
Meanwhile, in Table 5, it is concluded that the high yield for hydro-
genation of nitroarenes reaction is obtained. Compared entry 7 with
other entries, the electron induction effect reduces the rate of reaction.
However, for entries 8–10, the decrease of selectivity is due to the
demineralization. Herein, the perfectly catalytic performance and. the
incomparably bi-functional property of the catalyst are demonstrated.
Fig. 8. The recycles ability of the catalyst. (Reaction conditions: the catalyst
(20 mg), benzylalcohol (5 mmol) and benzylamine (4 mmol), solvent-free and
air with 15 mL/min at 120 °C for 3 h, conversion and selectivity were de-
termined by GC–MS.).
presents the different metallic catalysts. Obviously, FeCu@NPC-850
catalyst is different with other metal-based catalysts and metal oxide-
based catalysts in the N-alkylated reaction with solvent-free condition
as to the conversion and yield, the yield could reach 99.9%. From
Table 2, comparing with Entry 1–3 with Entry 4–6, it is clearly seen that
bimetallic catalysts are better than single metallic catalysts, there is no
doubt in conversion and selectivity. The results of entries 1–3 indicate
that metallic copper doped in NPC can effectively improve the con-
version rate, and magnetic metal in NPC can be highly selective. And
entries 7 and 8 explained that NeC bonds work in N-alkylated reaction
compared with graphite powder. The CuFe2O4 and CuCo3O5 catalysts
(entries 10 and 11) were obtained via the calcination of FeCu@NPC-
850 and CoCu@NPC-850 catalyst at 400 °C for 60 min in muffle fur-
nace. Obviously, compared entries 1 with 16, 17, 18, 19 and 20, metal-
N activity sites played an important role in the N-alkylated reaction.
Therefore, it is strong evidence prove the main active sites is Fe-N and
Cu-N, which synergistically promote the reaction processing. Mean-
while, it was also found that the optimum catalyst FeCu@NPC-850 can
be used in hydrogenation of nitroarenes. The N-alkylated reaction and
nitroarenes reduction were performed over FeCu@NPC-850 to screen
the optimum reaction conditions [56]. Primarily, benzylalcohol and
benzylamine were regarded as the N-alkylated reaction model sub-
strate, and nitroarenes served as the hydrogenation reaction model
substrate. The optimum reaction time, temperature, and the molar ratio
of these two reaction were tested. As is seen in Fig. 6(a), with the
temperature increasing from 90 to 130 °C, the conversion of reaction
firstly increased remarkably and then decreased sharply. So the opti-
mized temperature was determined to be 120 °C. To investigate the
effect of reaction time, the products existed in the reaction system from
0.5 to 3.5 h were analyzed. The results are presented in Fig. 6(b), the
conversion of the reactants was improved with increasing the reaction
time. Hence, the optimum reaction time was determined as 3 h. The
3.3. Kinetic study
In order to investigate the order of the reaction, one of the reactants
in the reaction system was needed to be far excessive. That is to say the
molar ratio of benzylamine and benzylalcohol are 10:0.1, 10:0.15,
10:0.2, 10:0.25 and 10:0.3 at 100 °C for 15 min with air (15 mL/min).
And the molar ratio of benzylalcohol and benzylamine is 3:0.2, 3:0.25,
3:0.3, 3:0.35 and 3:0.4 at the same reaction condition. The overall ki-
netics equation of the reaction can be defined as:
K
[alcohol] + [amine] + [O2] → [N − alkylated imines]+H2O
(1)
The formulation of the reaction rate is given by Eq. (2). Where the
[SA] and [SB] represents the benzylalcohol and benzylamine, K re-
presents the rate constant, and the a and b are the series of the [SA] and
[SB]. And it is assumed that the excessive reactant was neglected. The
formulation of the reaction rate is given by Eqs. (3) and (4), where the
k1 and k2 also represent the rate constants.
r = KCSa CSb
(2)
A
B
r = k1CSa
(3)
(4)
A
r = k2CSb
B
Then, the value of the reaction velocity and the value of equilibrium
Table 6
Comparative chart of catalytic activity of FeCu@NPC with other reported catalysts.
Entry
Catalyst
Amine dosage
(mmol)
Time (h)
Temp.
(oC)
Ea
Yield of
N-alkylated (%)
Reference
(kJ/mol)
1
2
3
4
5
6
7
8
FeCu@NPC-850
PdZn@Al2O3
CeO2
Cp*Ir(NHC)Cl2
Ni(OTf)2
CoCl2·6H2O/PPh3
Au-TiO2
[Cp*IrCl2]2
/K2CO3
4
1
0.05
1
–
1
–
1
3
120
110
30
110
120
140
25
55.52
56
–
–
–
–
–
–
99.9
99
99
93
99
72
90
88
This work
0.6
24
16
24
24
4
17
110
9
Ru3(CO)12
1
24
110
–
90
50