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Listar por autor "Zanón González, Raquel"

Mostrando ítems 1-5 de 5

Direct conversion of methane to aromatics in a catalytic co-ionic membrane reactor

Hernández Morejudo, Selene; Zanón González, Raquel; Escolástico Rozalén, Sonia; Yuste Tirados, I.; Malerod Fjeld, Harald; Vestre, P. K.; Coors, W. G.; Martinez Feliu, Agustin; Norby, T.; Serra Alfaro, José Manuel; Kjolseth, C. (American Association for the Advancement of Science, 2016-08-05)

[EN] Nonoxidative methane dehydroaromatization (MDA: 6CH(4) <-> C6H6 + 9H(2)) using shape-selective Mo/zeolite catalysts is a key technology for exploitation of stranded natural gas reserves by direct conversion into ...
Estudio de deshidoaromatización de metano sobre catalizadores 3%mo/hzsm-5 y permeación de hidrogeno a través de membranas La6W012

Zanón González, Raquel (Universitat Politècnica de València, 2016-01-18)

[EN] Study of methane dehydroaromatization on 3%Mo/HZSM-5 catalysts at 700°C and 0.207 bar, and occasionally at higher temperature (750°C). Hydrogen permeation through ceramic membranes made of La6W012 was investigated ...
Intensification of methane dehydroaromatization process on catalytic reactors

Zanón González, Raquel (Universitat Politècnica de València, 2017-06-19)

The present thesis has focused on the intensive study of the methane dehydroaromatization process under non-oxidative conditions for producing benzene and H2 in a direct way. Nevertheless, MDA process is thermodynamically ...
Proyecto de una planta para el control de esmaltabilidad de aceros en Sidmed-Arcelor

Zanón González, Raquel (Universitat Politècnica de València, 2014-03-28)

Consulta en la Biblioteca ETSI Industriales (5896)
Thermo-electrochemical production of compressed hydrogen from methane with near-zero energy loss

Malerød-Fjeld, H.; Clark, D.; Yuste Tirados, Irene; Zanón González, Raquel; Catalán-Martínez, David; Beeaff, D.; Hernández Morejudo, Selene; Vestre, P.K.; Norby, T.; Haugsrud, R.; Serra Alfaro, José Manuel; Kjølseth, C. (Nature Publishing Group, 2017-12)

[EN] Conventional production of hydrogen requires large industrial plants to minimize energy losses and capital costs associated with steam reforming, water-gas shift, product separation and compression. Here we present a ...