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conditions of the first step indicated that 1a was fully converted to
2a after 1 h at 80 °C with 1.05 equivalents of 2,5-DMTHF. There-
fore, the investigation focused on the second step with regard to
additive, additive amount, catalyst loading, and temperature. The
impact of additive on the formation of 4aa was initially explored
(entries 1–5). A series of different amines were used for the trans-
formation, and DABCO emerged as the best candidate, producing
4aa in 62% yield (entry 4). We hypothesized that the amine could
be involved in the decarboxylation or the Pictet-Spengler typed
rearomatization step [45,46]. The amount of DABCO displayed a
remarkable impact on the transformation (entries 7–9). Noted that
only 6% yield of 4aa was obtained in the absence of base, while
using 1.5 equivalents of DABCO afforded 77% yield (please see
the Supporting Information for full optimization). The quantity of
FeMoSe catalyst was crucial with regard to the formation of 4aa
(entries 10 and 11). Using less than 2.5 mol% of the catalyst plum-
metted the yield of 4aa. Only 7% yield was detected in the absence
of FeMoSe, proving the importance of the catalyst. A clean mixture
was obtained if 2.5 equivalents of phenylacetic acid was used
(entry 12). Running the reaction at lower temperature (than
140 °C) afforded low yield of 4aa (entry 13). Lastly, 4 h was enough
for the second step to get a considerable amount of 4aa (entries 14
and 15). With the conditions in hand, we attempted to conduct the
reaction on a large scale. In the 2 mmol run, 74% yield of 4aa was
obtained, showing that the reacion is scalable (Scheme 2).
As the synthesis of 4aa from 1a, 2,5-DMTHF, and 3a via one-pot
strategy utilizing the FeMoSe catalyst was conducted in liquid
phase, the potentiality that 4aa might be formed via homogeneous
catalysis was investigated. In some cases, the solid catalyst might
be partially soluble in the reaction medium during the catalytic
experiment, and leached species might be active for the transfor-
mation. In order to clarify if leached species, if any, contributed
to the formation of 4aa, a control experiment was consequently
performed. The reaction was carried out under standard conditions
for 4 h. After that, the reaction mixture was diluted by ethyl acet-
ate, and then analyzed by GC. The solid catalyst was removed by
filtration. The filtrate was subsequently concentrated under vac-
uum prior to be used for the next catalytic experiment. Following
this, 1a, 2,5-DMTHF, and 3a were added, and the transformation
was allowed to proceed under standard conditions in the absence
of utilizing the FeMoSe catalyst. The formation of 4aa during the
course of the reaction was monitored by GC. To our expect, only
4% yield of 4aa was detected for the transformation after 4 h
(Fig. 3). The results verified that the one-pot reaction of 1a, 2,5-
DMTHF, and 3a to form 4aa using the FeMoSe catalyst was truly
heterogeneous.
Fig. 3. Leaching test.
2,5-DMTHF, 2.5 equivalents of 3a, 1.5 equivalents of DABCO, in
the presence of 2.5 mol% catalyst as previously described. Upon
completion of the experiment, the FeMoSe powder was separated
from the reaction mixture by a simple centrifugation, washed thor-
oughly with excess amounts of methanol, dried under strong vac-
uum for 2 h, and reused in the next catalytic run under standard
conditions. It was noted that the FeMoSe catalyst was reusable
without a major loss of catalytic activity. Certainly, 88% yield of
4aa was obtained in the 6th catalytic run (see Fig. 4).
Morphology and chemical composition of the FeMoSe catalyst
collected after catalytic assay were characterized to gain insights
into its eventual changes during the catalytic transformation.
SEM analysis revealed the similar morphology (Fig. 1e) to that
recorded for the as-prepared FeMoSe catalyst (Fig. 1a, b). FeMoSe
nanosheets as well as its agglomeration in form of large nanopar-
ticles were remained after being used in the catalysis. However,
To highlight significant aspects of using the FeMoSe catalyst for
the synthesis of 4aa from 1a, 2,5-DMTHF, and 3a via one-pot strat-
egy, the reusability of the catalyst was studied. Previously, the cat-
alysts used in the synthesis of 4aa from 2a were not recyclable
[11–17]. Therefore, exploring a recyclable heterogeneous catalyst
for the formation of 4aa to facilitate product purification and to
minimize waste would add a prominent value to the one-pot
strategy. The reaction was conducted using 1.05 equivalent of
Fig. 4. Reuse of the FeMoSe catalyst in the synthesis of 4-phenylpyrrolo[1,2-a]
quinoxaline.
Scheme 2. Synthesis of 4-phenylpyrrolo[1,2-a]quinoxaline at 2 mmol scale.