TY - JOUR
T1 - Continuously operated hydroamination - Toward high catalytic performance via organic solvent nanofiltration in a membrane reactor
AU - Vogelsang, Dennis
AU - Dreimann, Jens M.
AU - Wenzel, Dominik
AU - Peeva, Ludmila
AU - Burgal, Joao da Silva
AU - Livingston, Andrew G.
AU - Behr, Arno
AU - Vorholt, Andreas J.
N1 - Funding Information:
This work is part of the Sonderforschungsbereich/Transregio 63 “Integrated Chemical Processes in Liquid Multiphase Systems” (TRR63). The authors would like to thank the Deutsche Forschungsgemeinschaft (DFG) for financial support.
Publisher Copyright:
© 2017 American Chemical Society.
Copyright:
Copyright 2017 Elsevier B.V., All rights reserved.
PY - 2017/11/22
Y1 - 2017/11/22
N2 - Still, the hydroamination of dienes to form allylic amines is a challenging task in a continuous operation. Herein, we present the performance of a membrane reactor by the implementation of a continuously operated hydroamination reaction of β-myrcene with morpholine. Via application of a poly ether-ether-ketone (PEEK) membrane, operation at elevated temperatures was possible in an integrated reaction/separation unit. First, the kinetics of the hydroamination reaction and relevant membrane characteristics were determined under optimized reaction conditions. Afterward, these results were incorporated in a reactor/separator model to predict the process behavior. With this, catalyst replenishment was adjusted resulting in stable continuous operation. In the end an increase of the turnover number from 460 to 5135 compared to a batch process was achieved. The desired geranyl amines were obtained in very good yields higher than 80%, while an excellent conversion of β-myrcene above 93% was reached in a long-time stable process.
AB - Still, the hydroamination of dienes to form allylic amines is a challenging task in a continuous operation. Herein, we present the performance of a membrane reactor by the implementation of a continuously operated hydroamination reaction of β-myrcene with morpholine. Via application of a poly ether-ether-ketone (PEEK) membrane, operation at elevated temperatures was possible in an integrated reaction/separation unit. First, the kinetics of the hydroamination reaction and relevant membrane characteristics were determined under optimized reaction conditions. Afterward, these results were incorporated in a reactor/separator model to predict the process behavior. With this, catalyst replenishment was adjusted resulting in stable continuous operation. In the end an increase of the turnover number from 460 to 5135 compared to a batch process was achieved. The desired geranyl amines were obtained in very good yields higher than 80%, while an excellent conversion of β-myrcene above 93% was reached in a long-time stable process.
UR - http://www.scopus.com/inward/record.url?scp=85035015422&partnerID=8YFLogxK
U2 - 10.1021/acs.iecr.7b03770
DO - 10.1021/acs.iecr.7b03770
M3 - Article
AN - SCOPUS:85035015422
SN - 0888-5885
VL - 56
SP - 13634
EP - 13641
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 46
ER -