Zobrazeno 1 - 4
of 4
pro vyhledávání: '"Leonardo José Lins Maciel"'
Autor:
Emerson Cristofer Kohlrausch, Denilson de Vasconcelos Freitas, Cícero Inácio da Silva Filho, Lara Fernandes Loguercio, Larissa A. Santa-Cruz, Leonardo José Lins Maciel, Maria Zilda Oliveira, Calink Indiara do Livramento dos Santos, Giovanna Machado
Publikováno v:
Energy Technology. 11
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::d3d00359c82122d7e9bcf502da959508
https://doi.org/10.1002/ente.202200676
https://doi.org/10.1002/ente.202200676
Autor:
Leonardo José Lins Maciel, Augusto Knoechelmann, Cesar Augusto Moraes de Abreu, Aleksándros El Áurens Meira de Souza, Valderio O. Cavalcanti-Filho
Publikováno v:
Reaction Kinetics, Mechanisms and Catalysis. 101:407-416
The conversion of natural gas was carried out via tri-reforming of methane in a fixed bed reactor employing a Ni/γ-Al2O3 catalyst. The kinetic evaluations were performed in a temperature range from 923 to 1,123 K under atmospheric pressure. The effe
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::b23ad8663010e74ee104024a33fed0c6
https://doi.org/10.1007/s11144-010-0232-9
https://doi.org/10.1007/s11144-010-0232-9
Autor:
Cesar Augusto Moraes de Abreu, Leonardo José Lins Maciel, Valderio O. Cavalcanti-Filho, Aleksándros El Áurens Meira de Souza, Nelson Medeiros de Lima Filho
Publikováno v:
Industrial & Engineering Chemistry Research. 50:2585-2599
A reforming experiment was performed using a nickel catalyst, with the goal of suggesting a mechanism for the autothermal reforming of methane (ATR), under thermally neutral conditions. To bring the process to future scale-up at a fixed-bed reactor,
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::0c0df3deb76eeb2b29628199ceed2442
https://doi.org/10.1021/ie100637b
https://doi.org/10.1021/ie100637b
Autor:
Cesar Augusto Moraes de Abreu, Solange Maria de Vasconcelos, Leonardo José Lins Maciel, Augusto Knoechelmann, Aleksándros El Áurens Meira de Souza
Dry reforming with partial oxidation of natural gas to syngas process with nickel catalysts supported on γ-alumina was compared with a dry reforming process, where methane conversion and the hydrogen and carbon monoxide yields at 1023 K, 1073 K and
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::0bb6e3ba0c0455615c2c24053d0e3ee4
https://doi.org/10.1016/s0167-2991(07)80176-5
https://doi.org/10.1016/s0167-2991(07)80176-5
