Zobrazeno 1 - 10
of 14
pro vyhledávání: '"Noemi S. Schbib"'
Autor:
Marisa Noemi Pedernera, Daniel Oscar Borio, Eduardo Lopez, Yanina Marianela Bruschi, Noemi S. Schbib
Publikováno v:
International Journal of Hydrogen Energy. 37:14887-14894
The ethanol steam reforming (ESR) is studied in a parallel plate reactor with square channels of 500-2000 μm and washcoated with Pd-based catalyst. The endothermic process is co- or countercurrently heated by means of a flue gas stream flowing throu
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::e7566ffd3c49d085732ccf24ce2debce
https://doi.org/10.1016/j.ijhydene.2012.01.175
https://doi.org/10.1016/j.ijhydene.2012.01.175
Autor:
Andrés M. Anzola, Daniel Oscar Borio, Marisa Noemi Pedernera, Noemi S. Schbib, Yanina Marianela Bruschi, Eduardo López
Publikováno v:
Industrial & Engineering Chemistry Research. 50:2698-2705
A simulation study of a microreactor for steam reforming of ethanol (ESR) over a washcoated Pd catalyst is reported in the present manuscript. Both co- and countercurrent configurations are considered for the streams of reactants and flue gas through
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::b905cff25f04323d3139cf9c6e2cc432
https://doi.org/10.1021/ie100739m
https://doi.org/10.1021/ie100739m
Publikováno v:
Industrial & Engineering Chemistry Research. 40:5215-5221
The influence of the heat-flux axial profiles on the main variables of an industrial primary steam reformer (i.e., outlet methane conversion, process gas temperature, tube-skin temperature, and equilibrium approach) has been studied. By means of adju
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::27aa68e0effdfa7c0dde142b897a988a
https://doi.org/10.1021/ie001065d
https://doi.org/10.1021/ie001065d
Publikováno v:
Industrial & Engineering Chemistry Research. 40:5199-5205
This work focuses on the study of the influence of the methane combustion kinetics on the operation of an autothermal catalytic reactor for heat generation (domestic scale). The feed (methane and air) is preheated by means of a direct heat exchange b
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::b577452016e3cc509207b5001653b1e8
https://doi.org/10.1021/ie001063t
https://doi.org/10.1021/ie001063t
Publikováno v:
Computers & Chemical Engineering. 23:S783-S786
The steady, state simulation and optimization of a large-scale ammonia converter is considered. The reactor consists of two adiabatic radial-flow catalyst beds in series with interstage cooling. The feed stream is preheated in an interbed heat exchan
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::c3c50e6cdc107eb8b35a1bf0ff3cdb47
https://doi.org/10.1016/s0098-1354(99)80192-6
https://doi.org/10.1016/s0098-1354(99)80192-6
Publikováno v:
Chemical Engineering Science. 54:1313-1318
The unsteady state simulation of a set of industrial fixed-bed reactors is presented. The catalytic dehydrogenation of 1-butene into 1,3-butadiene is selected as case study. These reactors operate under reaction-regeneration cycles. Each stage of the
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::2c3b03e36450c513925f5facdac4e423
https://doi.org/10.1016/s0009-2509(99)00064-0
https://doi.org/10.1016/s0009-2509(99)00064-0
Publikováno v:
Industrial & Engineering Chemistry Research. 35:1496-1505
The kinetics of acetylene hydrogenation in the presence of a large excess of ethylene was studied in a laboratory flow reactor. Experiments were carried out using a Pd/α-Al2O3 commercial catalyst a...
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::f664432711e2ff9e2182234e6685a5d6
https://doi.org/10.1021/ie950600k
https://doi.org/10.1021/ie950600k
Autor:
Daniel Oscar Borio, Noemi S. Schbib
Publikováno v:
Computers & Chemical Engineering. 19:345-350
The simulation and optimization of a set of industrial fixed bed catalytic reactors is presented. The reactors are operating in deactivation-regeneration cycles. Dynamic mathematical models for the four stages of the process are included, i.e. dehydr
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::0f0ceddf8384e6d4d65ee545c488ebcb
https://doi.org/10.1016/0098-1354(95)87061-x
https://doi.org/10.1016/0098-1354(95)87061-x
Publikováno v:
Computers & Chemical Engineering. 18:S355-S359
The dynamic simulation of a frontal industrial acetylene converter and its closed-loop performance under three different control strategies are discussed in the present work. The reactor is used for the selective hydrogenation of acetylene in the pre
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::160ec4bc8c0e653f8f78c373331c9f7c
https://doi.org/10.1016/0098-1354(94)80059-6
https://doi.org/10.1016/0098-1354(94)80059-6
This study reports a comprehensive multiphase gas-solid dynamic mathematical model that successfully describes the batch growth of silicon particles in a CVD submerged spouted bed reactor. This multiphase reactor model takes into account the hydrodyn
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::2180938eb56067a8a3f8f309e7ddb0ec
https://www.degruyter.com/view/j/ijcre.2006.4.1/ijcre.2006.4.1.1306/ijcre.2006.4.1.1306.xml?format=INT
https://www.degruyter.com/view/j/ijcre.2006.4.1/ijcre.2006.4.1.1306/ijcre.2006.4.1.1306.xml?format=INT
