Zobrazeno 1 - 10
of 10
pro vyhledávání: '"Catarina G. Braz"'
Publikováno v:
Energy. 278:127673
The supply, storage, and (international) transport of green hydrogen (H2) are essential for the decarbonization of the energy sector. The goal of this study was to assess the final cost-price and carbon footprint of imported green H2 in the market vi
Autor:
Nicole Lutters, Henrique A. Matos, Jorge Rocha, Eugeny Y. Kenig, Ricardo Alvim, Catarina G. Braz
Publikováno v:
Industrial & Engineering Chemistry Research. 59:5996-6006
Although the absorption of formaldehyde is a crucial stage within its production process, the number of models available in the literature is limited. The complexity of the absorption of formaldehy...
Publikováno v:
Computer Aided Chemical Engineering ISBN: 9780323958790
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::5a63d6eae841cacf999111e9c01b34f7
https://doi.org/10.1016/b978-0-323-95879-0.50188-0
https://doi.org/10.1016/b978-0-323-95879-0.50188-0
Autor:
Catarina G. Braz, Ali Najarnezhadmashhadi, Vincenzo Russo, Kari Eränen, Henrique A. Matos, Tapio Salmi
Publikováno v:
Computer Aided Chemical Engineering ISBN: 9780323958790
A comprehensive multiphase model was developed for a trickle bed reactor with solid foam packings. Three-dimensional dynamic mass and energy balances in the three phases of heterogeneously catalysed reaction systems were implemented, and the mass and
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::55196907c0d049cbe0d057f7fdb2ea35
https://doi.org/10.1016/b978-0-323-95879-0.50013-8
https://doi.org/10.1016/b978-0-323-95879-0.50013-8
Autor:
Ali Najarnezhadmashhadi, Catarina G. Braz, Vincenzo Russo, Kari Eränen, Henrique A. Matos, Tapio Salmi
An advanced comprehensive and transient multiphase model for a trickle bed reactor with solid foam packings was developed. A new simulation model for isothermal three-phase (gas–liquid–solid) catalytic tubular reactor models was presented where a
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::9ead2553522405b576e67d13269424c1
https://hdl.handle.net/11588/895073
https://hdl.handle.net/11588/895073
This work aimed at the development of a model of an industrial formaldehyde production plant, to identify the process variables that will have the most impact in the improvement of the process efficiency and the increase of its profitability. The mod
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::10c0e9d531f4af52d24656807d8b5b1d
https://doi.org/10.1016/b978-0-12-823377-1.50052-5
https://doi.org/10.1016/b978-0-12-823377-1.50052-5
Publikováno v:
Repositório Científico de Acesso Aberto de Portugal
Repositório Científico de Acesso Aberto de Portugal (RCAAP)
instacron:RCAAP
Repositório Científico de Acesso Aberto de Portugal (RCAAP)
instacron:RCAAP
In the present work, a first-principles model of methanol partial oxidation to formaldehyde in an industrial reactor was developed and the reaction kinetic and deactivation parameters estimated, taking advantage of the temperature profile established
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::82e750367353b58f47a149e0863522d1
This work focused on the simulation of an industrial system of formaldehyde absorption columns. For this purpose, a rate-based stage model of the system subjected to study was developed in gPROMS® Modelbuilder 4.2.0 and the simulation results compar
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::ec4d6aeee639999faf723262968ea4e5
https://doi.org/10.1016/b978-0-444-64235-6.50007-3
https://doi.org/10.1016/b978-0-444-64235-6.50007-3
This work focussed on the deactivation of molybdenum oxide installed in an industrial methanol oxidation reactor. The deactivation parameters were estimated using the operational data obtained during the entire lifetime of the previously installed ca
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=od______1406::eac9294e475d70abacf8c9027f437dbc
https://hdl.handle.net/10216/116568
https://hdl.handle.net/10216/116568
This work focussed on the deactivation of molybdenum oxide installed in an industrial methanol oxidation reactor. The deactivation parameters were estimated using the operational data obtained during the entire lifetime of the previously installed ca
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::f190b0305befcde48166454000384d67
https://doi.org/10.1016/b978-0-444-63965-3.50022-2
https://doi.org/10.1016/b978-0-444-63965-3.50022-2