Zobrazeno 1 - 7
of 7
pro vyhledávání: '"Laísse C.A. Maranhão"'
Autor:
David Merino, Oihane Sanz, Nelson Medeiros de Lima Filho, Cesar Augusto Moraes de Abreu, André T.S. Ribeiro, Rodrigo A.C. Bartolomeu, Mario Montes, Laísse C.A. Maranhão, Antonio O. S. Silva, Victor V.L. Bezerra, Giovanna Machado, Luciano C. Almeida
Publikováno v:
Fuel. 231:157-164
This article highlights the formulation and evaluation of Co-Ru catalysts on silica used in Fischer-Tropsch synthesis. An acid treatment of the support associated with the addition of sucrose as a chelating agent was employed. The six formulated cata
Autor:
Evelle D.C. Oliveira, Lívia N. Ribeiro, Luciano C. Almeida, André T.S. Ribeiro, Giovanna Machado, Aline C.S. Fonseca, Emerson F.M. da Silva, José Pacheco, Laísse C.A. Maranhão
Publikováno v:
Chemical Engineering and Processing - Process Intensification. 147:107792
A batch-process with a dispersed solid photocatalyst requires a large reactor and unit process for catalyst recovery, increasing the treatment cost. Structured-supported photocatalysts enable the use of continuous compact reactors that are photoactiv
Autor:
Cesar Augusto Moraes de Abreu, F. G. Sales, Nelson Medeiros de Lima Filho, Laísse C.A. Maranhão
Publikováno v:
Chemical Engineering Science. 62:5386-5391
The catalytic process of aldehyde production from alkaline lignin extracted from sugarcane bagasse was evaluated in a batch slurry reactor and operated in a continuous three-phase fluidized-bed reactor with a palladium catalyst, at the operating cond
Autor:
C. A. Moraes De Abreu, N. M. Lima Filho, J. E. B. Neto, Ana Catarina Lima, Laísse C.A. Maranhão
Publikováno v:
Anais do XX Congresso Brasileiro de Engenharia Química.
Autor:
Fernando G. Sales, Cesar Augusto Moraes de Abreu, Laísse C.A. Maranhão, Nelson Medeiros de Lima Filho
Publikováno v:
Industrial & Engineering Chemistry Research. 45:6627-6631
The catalytic wet air oxidation (CWAO) of lignin, obtained from sugar-cane bagasse, was evaluated through kinetic studies of the process of aromatic aldehyde production. The operations were carried...
Autor:
Cesar Augusto Moraes de Abreu, F. G. Sales, João Alexandre Ferreira da Rocha Pereira, Laísse C.A. Maranhão
Publikováno v:
Reaction Kinetics and Catalysis Letters. 81:169-175
Kinetic evaluations were accomplished in a discontinuous three-phase reactor for saccharose, glucose and fructose hydrogenations at 373, 393 and 413 K, and 24 atm. Selectivities attained values in the order of 99.05%. Langmuir-Hinshelwood models base
Publikováno v:
Brazilian Journal of Chemical Engineering, Volume: 22, Issue: 3, Pages: 443-452, Published: SEP 2005
Brazilian Journal of Chemical Engineering v.22 n.3 2005
Brazilian Journal of Chemical Engineering
Associação Brasileira de Engenharia Química (ABEQ)
instacron:ABEQ
Brazilian Journal of Chemical Engineering, Vol 22, Iss 3, Pp 443-452 (2005)
Brazilian Journal of Chemical Engineering v.22 n.3 2005
Brazilian Journal of Chemical Engineering
Associação Brasileira de Engenharia Química (ABEQ)
instacron:ABEQ
Brazilian Journal of Chemical Engineering, Vol 22, Iss 3, Pp 443-452 (2005)
The hydrodynamic parameters were determined for two different three-phase systems (fluidized-bed and trickle-bed) through the experimental evaluation of the dynamic residence time distribution in the gas or liquid phase. For different fluid phase flo
Externí odkaz:
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http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322005000300012&lng=en&tlng=en
http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322005000300012&lng=en&tlng=en