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formation is generally catalyzed by copper(I) salts and correspond-
ing complexes. On the other hand, the more stable copper(II) has
been also applied in the presence of a reductant, usually sodium
ascorbate [54,74,75]. Only recently copper(II)-catalyzed reactions
under reductant-free conditions have been reported [72,73,76,77].
Mechanistic investigations and DFT calculations have proved that
the active copper(I) species is formed as a result of copper(II)-
assisted oxidation of solvents such as MeOH, EtOH or i-PrOH
[73,78,79] or homocoupling of alkynes [80,81]. Beyond many useful
copper(I) and copper(II) complexes, NHC-copper(I) complexes have
been recently applied exhibiting a remarkable activity in CuAAC
reactions [78,79,82–86]. Unfortunately, NHC-copper(II) have never
been applied in this reaction before. To our delight, we present the
first example of an NHCCu(II)-catalyzed Huisgen reaction. As men-
tioned above, NHC-copper(II) complexes showed higher activity in
the CuAAC reaction. However, the exact nature of this behavior
could not be explained without a detailed mechanistic study, due
to the complicated mechanistic scenario of the CuAAC reaction.
Recent theoretical and experimental studies have proved that
dimeric or higher order copper species are involved [81,87–90].
amount. Also, recycling without using a reducing agent was per-
formed (Fig. 2).
It appears that catalysts 3 and 4 have a good activity in metha-
nol both with and without the addition of sodium ascorbate. The
activity of catalysts 3 and 4 decreased after each reuse, indicating
their deactivation during the catalytic processes. Furthermore, the
activity of the reused catalyst with regard to the amount of the cat-
alyst was studied (Fig. 2, columns B, C, and D). It appeared that the
best yields for catalyst 3 (after the second run – 63%, after the third
run – 46%) and for catalyst 4 (72% and 46%) were obtained when
20 mg (0.2/10) of the catalyst was used (Fig. 2, column B). It was
probably caused by the presence of the catalytic centres which
did not participate in the reaction during the first run. Therefore,
they were not deactivated and could be active in the next run.
The high yields in the first run were observed even in the absence
of sodium ascorbate (Fig. 2, column A, 86% and 80% for catalysts 3
and 4, respectively). In the second and the third run, the activity of
catalysts 3 and 4 was higher when sodium ascorbate was present
(Fig. 2, column B).
These results show that the catalyst is deactivated during the
reaction cycle. The mechanism of the deactivation needs to be fur-
ther investigated in order to develop more active catalysts.
2.4. The recycling
The magnetic solid phase allows quick and easy separation of
the immobilized catalysts. Due to the highest activity of complexes
3 and 4, only the recycling of these two catalysts was investigated.
After completion of the model reactions, the catalysts were sepa-
rated from the reaction mixtures, and then washed once with
water and three times with MeOH. After purification, the solvent
was evaporated and the catalyst was reused. Fig. 2 presents the
model reaction yields after each reuse in a relation to the catalyst
3. Characterization
3.1. Copper content measurements
The copper mass content was investigated by SEM/EDX (Fig. 3).
The results show that catalyst 4 contains more copper than catalyst
3 (9 and 6 %mass, respectively). This can be assigned to stronger
complexing properties of NHC precursor 2a. The copper content
in catalysts 1 and 2 was also investigated. Surprisingly, catalysts
1 and 2 presented higher copper ion mass content (17% for both
catalysts) than catalysts 3 and 4. This fact does not correspond
with the lower activity of complexes 1 and 2. Furthermore, the
copper content after each reuse was measured and the results
are presented in Fig. 3. The graph clearly shows that copper con-
tent in catalysts 3 and 4 decreases after each reuse. The differences
are slight but they significantly influence the activity of the cata-
lysts. After the first run yields drop down by half (Fig. 2, column
C). This decrease of the activity cannot be explained only by the
leakage of copper (the drop of the yield is not directly proportional
to the copper content decrease). Deactivation of the catalyst poi-
soned by reaction by-products is an alternative explanation. Fur-
ther experiments were performed without the use of any
additional reducing agent (i.e. sodium ascorbate). Results show a
similar decrease of the activity of the tested catalysts in the second
and the third reuse.
The Cu leakage was investigated by AAS spectroscopy. Gener-
ally, after the separation of the catalyst, the reaction mixture was
washed by water. The aqueous layer was then analyzed by Atomic
Absorption Spectroscopy.
The leakage of copper from catalysts 1 (65.34 mg/ml) and 2
(256.45 mg/ml) is much higher than from 3 (7.94 mg/ml) and 4
(2.22 mg/ml), indicating lower stability of copper(I) complexes in
comparison to their copper(II) analogues.
In some cases, the activity of an immobilized catalyst can be
influenced by the engagement of a catalytically active free metal,
which can be present in the reaction mixture due to leakage [91].
In such cases, the yield is proportional to the metal ion content
in the reaction mixture after the completion of the process. In
our research no such tendency for copper ion leakage is observed.
Furthermore, the yields are not directly influenced by the free
metal ion content (high leakages of copper ions from catalysts 1
and 2 do not cause high yields).
Fig. 2. Catalytic activity of MNP@NHC (3) (up) and MNP@NHC (4) (bottom) towards
propargyl alcohol and benzyl azide generated in situ click reaction, with different
benzyl bromide to catalyst (mmol/mg) ratios: (A) 0.2/10 without sodium ascorbate;
(B), (C) and (D) - 0.2/10, 0.2/5 and 0.2/2.5, respectively, with the addition of sodium
ascorbate.