Zobrazeno 1 - 10
of 14
pro vyhledávání: '"Alouisius Nicolaas Renee Bos"'
Autor:
Alouisius Nicolaas Renee Bos, G. Jonkers, Cornelius Johannes Schellekens, Peter A. A. Klusener, F. During, Elco Dick Hollander, A. Othman, Ingmar Hubertus Josephina Ploemen
Publikováno v:
Chemical Engineering Science. 62:5495-5502
Unique gas and liquid phase radioactive tracer experiments have been performed in horizontal cross-flow bubble column reactors of a commercial ethylbenzene oxidation plant. These experiments validated CFD modelling predictions, which in turn formed t
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::020538e6aa7f999c47c5fe9a10b62d6e
https://doi.org/10.1016/j.ces.2007.03.044
https://doi.org/10.1016/j.ces.2007.03.044
Publikováno v:
Industrial & Engineering Chemistry Research. 34:3808-3816
Reactor types for commercial-scale methanol-to-olefins (MTO) processes in the ethene mode, using a small-pore molecular-sieve catalyst, have been evaluated both qualitatively and quantitatively. A kinetic model has been developed via an iterative pro
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::f018323fa50ae786d77bef990e82c7bb
https://doi.org/10.1021/ie00038a018
https://doi.org/10.1021/ie00038a018
Publikováno v:
AIChE journal, 40(5), 862-869. Wiley-Blackwell
A novel perfectly mixed laboratory reactor for determining kinetics of heterogeneously catalyzed gas-phase reactions has been developed. Perfect mixing is achieved by circulating the gas in the reactor using an axial flow impeller in a well streamlin
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::16096dbfce3be94056401b02289ffbcb
https://doi.org/10.1002/aic.690400512
https://doi.org/10.1002/aic.690400512
Publikováno v:
Chemical Engineering Communications. 121:55-80
The steady state and dynamic behaviour of an adiabatic packed bed reactor for the selective hydrogenation of mixtures of ethyne and ethene is studied. A heterogeneous model with axial dispersion of heat is solved numerically by means of a fully impli
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::02e04cee0e63c9a3dec22201038dd4f2
https://doi.org/10.1080/00986449308936137
https://doi.org/10.1080/00986449308936137
Publikováno v:
Chemical Engineering Communications. 121:27-53
The steady state and dynamic behaviour of an adiabatic packed bed reactor for the selective hydrogenation of ethyne and ethene mixtures was studied experimentally. Different methods to achieve adiabatic conditions on a laboratory scale were tested. T
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::f29dc5d321606032b9cede62aad6992d
https://doi.org/10.1080/00986449308936136
https://doi.org/10.1080/00986449308936136
Publikováno v:
Chemical engineering and processing : process intensification, 32(1), 53-63. Elsevier
The kinetics of the hydrogenation of gas mixtures of ethyne and ethene on a commercial Pd catalyst was studied experimentally using a Berty reactor. The experimental conditions corresponded with typical industrial tail-end conditions, 0.3–1.3% C2H2
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::e7310faa6efd3e74024d77083d578779
https://doi.org/10.1016/0255-2701(93)87006-g
https://doi.org/10.1016/0255-2701(93)87006-g
Publikováno v:
Chemical engineering and processing : process intensification, 32(1), 1-7. Elsevier
A review of the kinetics and mechanism for the selective hydrogenation of ethyne and ethene on palladium catalysts is presented. The progress made in the last fifteen years is mainly discussed. It has become clear that the classical view, where the s
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::db4a8b39c31dfcfe688e2f13b77d8182
https://doi.org/10.1016/0255-2701(93)87001-b
https://doi.org/10.1016/0255-2701(93)87001-b
Publikováno v:
ChemInform. 24
A review of the kinetics and mechanism for the selective hydrogenation of ethyne and ethene on palladium catalysts is presented. The progress made in the last fifteen years is mainly discussed. It has become clear that the classical view, where the s
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::53b59054ad7a8b4ce8993cfa22983ff9
https://doi.org/10.1002/chin.199340340
https://doi.org/10.1002/chin.199340340
Publikováno v:
Chemical Engineering Communications. 99:139-153
In this paper we discuss the use of an approximated form of the mass balance equation for a tubular reactor in which a gas phase reaction is carried out. By means of three examples it is shown that if density variations are not taken into account in
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::d3fbef257c941bcf62535cfa8f098ac7
https://doi.org/10.1080/00986449108911584
https://doi.org/10.1080/00986449108911584
Publisher Summary Shell has coproduced propylene oxide (PO) and styrene using its proprietary styrene monomer propylene oxide (SMPO) process for three decades. Research, development, and plant trials have been performed on a continuous basis in order
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::ba445ae808d5610d260d3f34c8f39f1b
https://doi.org/10.1016/b978-0-444-53188-9.00013-4
https://doi.org/10.1016/b978-0-444-53188-9.00013-4
