Zobrazeno 1 - 9
of 9
pro vyhledávání: '"Alberto Cantu-Perez"'
Autor:
Michel Romero-Flores, Alejandro D. Tapia-Martínez, Alberto Cantu-Perez, Alejandro Montesinos-Castellanos, Karlo Mariella-González
Publikováno v:
Combustion Theory and Modelling. 24:1070-1089
Shuttle kilns are widely used in the sanitary ware industry. A key parameter to reduce energy consumption and increase their overall performance is temperature uniformity. Therefore, in this paper ...
Autor:
Jorge de-J. Lozoya-Santos, Andrea Cardenas-Romero, Alberto Cantu-Perez, Juan C. Tudon-Martinez
Publikováno v:
Journal of Thermal Science and Engineering Applications. 14
The current control system of an industrial box furnace usually uses a proportional-integral-derivative (PID) controller. Typically, this control system requires on-site tuning and specific heuristic knowledge, such that the furnace can have acceptab
Autor:
Enrique A. López-Guajardo, Alejandro Montesinos-Castellanos, Asterios Gavriilidis, Michel Romero-Flores, Krishna D.P. Nigam, Alberto Cantu-Perez
Publikováno v:
Chemical Engineering and Processing - Process Intensification. 157:108154
In the present study, the flow behaviour through different micro-herringbone channels configurations (1-peak, 2-peak, 1–2 alternated peak herringbone channel and a flow inversion geometry) have been numerically analysed as a mean of intensifying ma
Autor:
Alberto Cantu-Perez, Juan C. Tudon-Martinez, Andrea Cardenas-Romero, Jorge de J. Lozoya-Santos
Publikováno v:
Applied Thermal Engineering. 161:114153
A zero dimensional thermodynamic model (0D-model) is used to represent the conservation equations of energy in an industrial box furnace for designing purposes. Thus, this paper proposes a 0D model-based design approach for industrial box furnaces wh
Publikováno v:
Chemical Engineering Journal, 227, 34-41. Elsevier
Falling film microreactors are ideally suited for fast exothermic reactions due to their large surface to volume ratio (up to 20,000 m2/m3) which greatly intensifies mass transfer. Despite the enhanced mass transfer characteristics of these reactors,
Autor:
Friedhelm Schönfeld, Dirk Ziegenbalg, Alberto Cantu-Perez, Ma’moun Al-Rawashdeh, Patrick Löb, Volker Hessel, Asterios Gavriilidis
Publikováno v:
Chemical Engineering Journal, 179, 318-329. Elsevier
The high liquid based specific interfacial area, up to ∼20,000 m 2 /m 3 , of falling film microreactors renders them to be ideally suited to carry out fast exothermic and mass transfer limited reactions. To understand the role of and control this i
Publikováno v:
Applied Thermal Engineering. 31:634-639
Residence time distributions (RTDs) have been investigated experimentally for reactors with straight and zig-zag channels. The channels are formed by microstructured plates placed on top of each other and containing obstacles and holes to allow flow
Publikováno v:
Chemical Engineering Journal. 160:834-844
Residence time distributions (RTD) have been determined numerically and experimentally for channels with and without herringbone structures. Computational fluid dynamics (CFD) and particle tracking with random walk diffusion were employed for the num
Autor:
Alberto Cantu-Perez, A. Ghaini, Mark D. Roydhouse, Achilleas Constantinou, William B. Motherwell, Asterios Gavriilidis
Reactions of n-decene with ozone and subsequent quenching of the formed ozonides were carried out under flow conditions using the standard Vapourtec flow system equipped with a cooled flow cell. The reactions were performed continuously and in the an
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::3443d2207c20aa57883a53296b0d0af0
https://hdl.handle.net/20.500.14279/23798
https://hdl.handle.net/20.500.14279/23798