catalysts
Article
Direct Amide Synthesis over Composite Magnetic Catalysts in a
Continuous Flow Reactor
Yawen Liu
1
and Evgeny V. Rebrov
1,2,
*
Citation: Liu, Y.; Rebrov, E.V. Direct
Amide Synthesis over Composite
Magnetic Catalysts in a Continuous
Flow Reactor. Catalysts 2021, 11, 146.
https://doi.org/10.3390/catal11020146
Received: 31 December 2020
Accepted: 16 January 2021
Published: 20 January 2021
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1
School of Engineering, University of Warwick, Coventry CV4 7AL, UK; liuyw.cn@hotmail.com
2
Department of Chemical Engineering and Chemistry, Eindhoven University of Technology,
5600MB Eindhoven, The Netherlands
* Correspondence: E.Rebrov@warwick.ac.uk
Abstract: Composite magnetic catalysts containing different amounts of sulfated titania (33–50 wt %)
have been prepared by means of high energy ball-milling between TiO
2
and NiFe
2
O
4
. The catalysts
have been characterized with N
2
adsorption/desorption isotherms, XRD, temperature programmed
oxidation (TPO) and vibrating sample magnetometer (VSM). The catalytic activity was measured
in the reaction of aniline and 4-phenylbutyric acid in the continuous mode under conventional and
inductive heating. The effect of catalyst loading in the reactor on reaction and deactivation has been
studied, indicating the catalyst containing 50 wt % titania gave the highest reaction rate and least
deactivation. The operation in a flow reactor under inductive heating increased the amide yield by
25% as compared to conventional heating. The initial reaction rate decreased by 30% after a period of
15 h on stream. The catalyst activity was fully restored after a treatment with an air flow at 400
◦
C.
Keywords: sulfated titania; composite magnetic catalysts; inductive heating; direct amide synthesis
1. Introduction
Amide synthesis is considered as one of the most important reactions in the pharma-
ceutical industry. At the moment, the reaction is mainly performed utilizing a coupling
agent [1], resulting in low atom-economy [2]. Direct amide synthesis over heterogeneous
catalysts, using an acid and an amine provides a green and atom efficient way to form the
amide bond. In addition, the catalyst can be easily recycled. Many heterogeneous catalysts
have been studied to catalyze the direct amide reaction, such as sulfated tungstate [3],
CeO
2
[4], SiO
2
[5] and Co based catalysts [6]. Sulfated TiO
2
demonstrated a very high
reaction rates and the yield of amides up to 90% at 115
◦
C in 12 h [7]. A nanostructured
sulfated titania catalyst with uniform size was synthesized by the hydrothermal sol–gel
method [8]. The amide yields over 75% were reported at a temperature of 110
◦
C. In our
previous work [9], composite magnetic catalyst containing sulfated TiO
2
also showed a
better catalytic performance in the direct amidation of 4-phenylbutyric acid and aniline
than those containing pure TiO
2
.
The reaction is carried out in a batch mode [6,7,10,11]. A continuous process has an
advantage of easy scale up compared to a batch process. Comerford et al. [12] developed
a continuous reactor packed with mesoporous structured silicas (SBA-15) or activated
chromatographic K60 silica catalyst to synthesize N-(phenyl)-phenylacetamide at 150
◦
C.
They used 12 mmol of each reagent (carboxylic acid and aniline) dissolved in toluene at an
initial concentration of 0.6 M. The production rate was 0.349 g h
−1
under optimized reaction
conditions. However, in the case of K60 silica, the loading of the catalyst required was very
high to obtain a noticeable amount of product. Britton et al. [13] developed a vortex fluidic
device (VFD) for amide synthesis at 60
◦
C. The reaction between cyclohexylamine and
butyrylchloride performed in the VFD provided the target amide in 94% yield in 80 s while
the same reaction in the batch mode resulted in 9% yield for the same reaction time. The
VFD operated at 6950 rpm enhancing the mixing of reactants on the microscale. While the
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