ST Yong, CW Ooi, SP Chai, XS Wu - International Journal of hydrogen …, 2013 - Elsevier
Recent development in proton-exchange membrane fuel cell technology has stimulated research in fuel processing for hydrogen production. Hydrogen can be produced from four …
J Zhao, R Shi, Z Li, C Zhou, T Zhang - Nano Select, 2020 - Wiley Online Library
Hydrogen production and storage as the core of novel hydrogen economy attract extensive attentions in both industry and academia. Methanol‐involved hydrogen production has been …
EV Matus, IZ Ismagilov, SA Yashnik… - International Journal of …, 2020 - Elsevier
Hydrogen production through autothermal reforming of methane (ATR of CH 4) over promoted Ni catalysts was studied. The control of the ability to self-activation and activity of …
A kinetic model has been established for the direct synthesis of dimethyl ether (DME) from syngas and CO 2 feeds. The kinetic parameters have been determined fitting the …
Y Zhang, T Wei, K Xu, Z Ren, L Xiao, J Song, F Zhao - RSC advances, 2015 - pubs.rsc.org
Two hollow CuFe2O4 nanospheres (CuFe2O4-p and CuFe2O4-d) were successfully prepared using a hydrothermal method. CuFe2O4-p has a smaller size and higher BET …
L Oar-Arteta, A Remiro, J Vicente, AT Aguayo… - Fuel processing …, 2014 - Elsevier
The study focuses on the regenerability of bifunctional catalysts prepared with different metallic functions (CuZnOAl 2 O 3 and CuFe 2 O 4 spinel) and HZSM-5 zeolite (SiO 2/Al 2 O …
AA Pechenkin, SD Badmaev, VD Belyaev… - Applied Catalysis B …, 2015 - Elsevier
Dimetoxymethane steam reforming (DMM SR) to hydrogen-rich gas over a bifunctional СuO– CeO 2/γ-Al 2 O 3 catalyst was studied. The performance of γ-Al 2 O 3, CeO 2/γ-Al 2 O 3, and …
L Oar-Arteta, A Remiro, AT Aguayo… - Industrial & …, 2015 - ACS Publications
A study is conducted on the effect the operating variables (temperature, space-time, steam/DME molar ratio, DME partial pressure) have on DME steam reforming over …
L Oar-Arteta, A Remiro, F Epron, N Bion… - Industrial & …, 2016 - ACS Publications
The kinetic behavior of noble metal catalysts (Pt and Rh supported on Al2O3/CeO2 mixed oxides) and of Cu catalysts (conventional CuO–ZnO–Al2O3 (CZA) catalyst and CuFe2O4 …