Development and Monitoring of a Continuous Polyurethane Pilot Reactor

The transition from batch to continuous polyurethane (PU) process is considered for process intensification. An integrated methodological and technological study is proposed. The development of the new process is based on modeling and product characteristics. In order to do so, the kinetics of the p...

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Published in:Chemical engineering & technology Vol. 33; no. 11; pp. 1900 - 1908
Main Authors: Nadjiadjim, G., Sheibat-Othman, N., Févotte, G., Dupuy, J.
Format: Journal Article
Language:English
Published: Weinheim WILEY-VCH Verlag 01-11-2010
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Abstract The transition from batch to continuous polyurethane (PU) process is considered for process intensification. An integrated methodological and technological study is proposed. The development of the new process is based on modeling and product characteristics. In order to do so, the kinetics of the polyaddition of polycaprolactone diol (polyol) and 4,4'‐diphenylmethane diisocyanate were studied and identified by using offline measurement of the diisocyanate concentration. Some characteristics of the final polymer were also investigated, such as the heat capacity and viscosity that affect the behavior of the continuous process. These results were used to design a tubular reactor for continuous production of PU. Since online monitoring of intensified processes is primordial, in situ near‐infrared spectroscopy was used to predict the concentration of free diisocyanate in real time. Process intensification is important in polymer production to ensure flexibility in switching from one polymer production to another, reproducibility, enhance mixing and heat transfer, and avoid losses due to changes in raw materials or deviations of the process compounds. Based on modeling and product characteristics the transition from batch to continuous production of polyurethanes was developed.
AbstractList The transition from batch to continuous polyurethane (PU) process is considered for process intensification. An integrated methodological and technological study is proposed. The development of the new process is based on modeling and product characteristics. In order to do so, the kinetics of the polyaddition of polycaprolactone diol (polyol) and 4,4'‐diphenylmethane diisocyanate were studied and identified by using offline measurement of the diisocyanate concentration. Some characteristics of the final polymer were also investigated, such as the heat capacity and viscosity that affect the behavior of the continuous process. These results were used to design a tubular reactor for continuous production of PU. Since online monitoring of intensified processes is primordial, in situ near‐infrared spectroscopy was used to predict the concentration of free diisocyanate in real time.
The transition from batch to continuous polyurethane (PU) process is considered for process intensification. An integrated methodological and technological study is proposed. The development of the new process is based on modeling and product characteristics. In order to do so, the kinetics of the polyaddition of polycaprolactone diol (polyol) and 4,4'‐diphenylmethane diisocyanate were studied and identified by using offline measurement of the diisocyanate concentration. Some characteristics of the final polymer were also investigated, such as the heat capacity and viscosity that affect the behavior of the continuous process. These results were used to design a tubular reactor for continuous production of PU. Since online monitoring of intensified processes is primordial, in situ near‐infrared spectroscopy was used to predict the concentration of free diisocyanate in real time. Process intensification is important in polymer production to ensure flexibility in switching from one polymer production to another, reproducibility, enhance mixing and heat transfer, and avoid losses due to changes in raw materials or deviations of the process compounds. Based on modeling and product characteristics the transition from batch to continuous production of polyurethanes was developed.
Author Sheibat-Othman, N.
Févotte, G.
Nadjiadjim, G.
Dupuy, J.
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Issue 11
Keywords polymerization
reactivities
functional-groups
Tubular reactor kinetics
Polyurethane
kinetic-model
linear polyurethanes
Process intensification
Kinetics
Near-infrared spectroscopy
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Snippet The transition from batch to continuous polyurethane (PU) process is considered for process intensification. An integrated methodological and technological...
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SubjectTerms Chemical and Process Engineering
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Kinetics
Near-infrared spectroscopy
Polyurethane
Process intensification
Tubular reactor kinetics
Title Development and Monitoring of a Continuous Polyurethane Pilot Reactor
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