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Synthesis of percarboxylic acids in microreactor

Ebrahimi, Fatemeh (2012-03-01)

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isbn 9789522652140.pdf (4.030Mb)
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Ebrahimi, Fatemeh
01.03.2012
Lappeenranta University of Technology

Acta Universitatis Lappeenrantaensis

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Julkaisun pysyvä osoite on
https://urn.fi/URN:ISBN:978-952-265-214-0

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Percarboxylic acids are commonly used as disinfection and bleaching agents in textile, paper, and
fine chemical industries. All of these applications are based on the oxidative potential of these
compounds. In spite of high interest in these chemicals, they are unstable and explosive chemicals,
which increase the risk of synthesis processes and transportation. Therefore, the safety criteria in the
production process should be considered. Microreactors represent a technology that efficiently
utilizes safety advantages resulting from small scale. Therefore, microreactor technology was used
in the synthesis of peracetic acid and performic acid. These percarboxylic acids were produced at
different temperatures, residence times and catalyst i.e. sulfuric acid concentrations. Both synthesis
reactions seemed to be rather fast because with performic acid equilibrium was reached in 4 min at
313 K and with peracetic acid in 10 min at 343 K.
In addition, the experimental results were used to study the kinetics of the formation of performic
acid and peracetic acid. The advantages of the microreactors in this study were the efficient
temperature control even in very exothermic reaction and good mixing due to the short diffusion
distances. Therefore, reaction rates were determined with high accuracy. Three different models
were considered in order to estimate the kinetic parameters such as reaction rate constants and
activation energies. From these three models, the laminar flow model with radial velocity
distribution gave most precise parameters.
However, sulfuric acid creates many drawbacks in this synthesis process. Therefore, a ´´greener´´
way to use heterogeneous catalyst in the synthesis of performic acid in microreactor was studied. The cation exchange resin, Dowex 50 Wx8, presented very high activity and a long life time in this
reaction. In the presence of this catalyst, the equilibrium was reached in 120 second at 313 K which
indicates a rather fast reaction.
In addition, the safety advantages of microreactors were investigated in this study. Four different
conventional methods were used. Production of peracetic acid was used as a test case, and the safety
of one conventional batch process was compared with an on-site continuous microprocess. It was
found that the conventional methods for the analysis of process safety might not be reliable and
adequate for radically novel technology, such as microreactors. This is understandable because the
conventional methods are partly based on experience, which is very limited in connection with
totally novel technology.
Therefore, one checklist-based method was developed to study the safety of intensified and novel
processes at the early stage of process development. The checklist was formulated using the concept
of layers of protection for a chemical process. The traditional and three intensified processes of
hydrogen peroxide synthesis were selected as test cases. With these real cases, it was shown that
several positive and negative effects on safety can be detected in process intensification. The
general claim that safety is always improved by process intensification was questioned.
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PL 20
53851 Lappeenranta
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