TY - JOUR
T1 - Experimental and modelling study of partial oxidation of ethanol in a micro-reactor using gold nanoparticles as the catalyst
AU - Behravesh, Erfan
AU - Kilpiö, Teuvo
AU - Russo, V.
AU - Eränen, Kari
AU - Salmi, Tapio
N1 - tk.
PY - 2018
Y1 - 2018
N2 - A microreactor was used to oxidize ethanol to valuable products under atmospheric pressure. Nano-sized gold on alumina was used as heterogeneous catalyst in the microreactor. A uniform and stable catalyst coating in the microchannels was achieved by suspension method. The catalyst was characterized by transmission electron microscopy, X-ray photoelectron spectroscopy, energy dispersive X-ray analysis, nitrogen-physisorption and X-ray diffraction.The reaction system was studied by changing the operation conditions, i.e. the residence time and temperature (100–250 °C). The product stream was analyzed by on-line gas chromatography. The identified products were acetaldehyde, ethyl acetate, diethyl ether and ethylene. The aim of the study was to find out the operation conditions that favored the generation of the desired product. A detailed modelling work was included. A kinetic model was developed for the reaction system. Dynamic mass balance-based generic modelling was applied to estimate the rate parameters. gPROMs ModelBuilder, a highly advanced process modelling tool was used. The obtained selectivity for acetaldehyde formation was around 90% already at low temperatures. The mathematical model described the ethanol conversion and acetaldehyde selectivity very well. The experimental equipment, the catalyst, and the modelling approach are applicable for other gas-phase oxidation studies.
AB - A microreactor was used to oxidize ethanol to valuable products under atmospheric pressure. Nano-sized gold on alumina was used as heterogeneous catalyst in the microreactor. A uniform and stable catalyst coating in the microchannels was achieved by suspension method. The catalyst was characterized by transmission electron microscopy, X-ray photoelectron spectroscopy, energy dispersive X-ray analysis, nitrogen-physisorption and X-ray diffraction.The reaction system was studied by changing the operation conditions, i.e. the residence time and temperature (100–250 °C). The product stream was analyzed by on-line gas chromatography. The identified products were acetaldehyde, ethyl acetate, diethyl ether and ethylene. The aim of the study was to find out the operation conditions that favored the generation of the desired product. A detailed modelling work was included. A kinetic model was developed for the reaction system. Dynamic mass balance-based generic modelling was applied to estimate the rate parameters. gPROMs ModelBuilder, a highly advanced process modelling tool was used. The obtained selectivity for acetaldehyde formation was around 90% already at low temperatures. The mathematical model described the ethanol conversion and acetaldehyde selectivity very well. The experimental equipment, the catalyst, and the modelling approach are applicable for other gas-phase oxidation studies.
KW - Chemical Reactions Engineering
KW - Chemical Reactions Engineering
KW - Chemical Reactions Engineering
U2 - 10.1016/j.ces.2017.11.011
DO - 10.1016/j.ces.2017.11.011
M3 - Artikel
SN - 0009-2509
VL - 176
SP - 421
EP - 428
JO - Chemical Engineering Science
JF - Chemical Engineering Science
ER -