INVESTIGADORES
BORIO daniel Oscar
artículos
RODRÍGUEZ, M.L.; CADÚS, L.E.; BORIO, D.O.
Effect of heat losses on monolithic reactors for VOC abatement
CHEMICAL ENGINEERING JOURNAL; Año: 2019 vol. 377
DUCKWEN A.C., MORENO M.S., BORIO D.O., BANDONI J.A.
Disjunctive Optimization Model for the Production Planning and Blending of Crude Oil in a Conventional Oil Field
INDUSTRIAL & ENGINEERING CHEMICAL RESEARCH; Año: 2018 vol. 57 p. 653 - 665
ADROVER, MARÍA ESPERANZA; BORIO, DANIEL; PEDERNERA, MARISA
Comparison between WGS membrane reactors operating with and without sweep gas: Limiting conditions for co-current flow
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY; Año: 2017 vol. 42 p. 5139 - 5149
RODRÍGUEZ, M. LAURA; CADÚS, LUIS E.; BORIO, DANIEL O.
Monolithic reactor for VOCs abatement: Influence of non-uniformity in the coating
Journal of Environmental Chemical Engineering; Año: 2017 vol. 5 p. 292 - 302
IZURIETA, EDUARDO M.; BORIO, DANIEL O.; PEDERNERA, MARISA N.; LÓPEZ, EDUARDO
Parallel plates reactor simulation: Ethanol steam reforming thermally coupled with ethanol combustion
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY; Año: 2017 vol. 42 p. 18794 - 18804
Y. M. BRUSCHI; E. LÓPEZ; M. N. PEDERNERA; D. O. BORIO
Coupling exothermic and endothermic reactions in an ethanol microreformer for H2 production
CHEMICAL ENGINEERING JOURNAL; Lugar: Amsterdam; Año: 2016 vol. 294 p. 97 - 104
M. L. RODRÍGUEZ; L. E. CADÚS; D. O. BORIO
VOCS ABATEMENT IN ADIABATIC MONOLITHIC REACTORS: HEAT EFFECTS, TRANSPORT LIMITATIONS AND DESIGN CONSIDERATIONS
CHEMICAL ENGINEERING JOURNAL; Lugar: Amsterdam; Año: 2016
ESPINAL R.; ANZOLA A.; ADROVER E.; ROIG M.; CHIMENTAO R.; MEDINA F. ; LÓPEZ E. ; BORIO D.O.; LLORCA J.
Durable ethanol steam reforming in a catalytic membrane reactor at moderate temperature over cobalt hydrotalcite
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY; Lugar: Amsterdam; Año: 2014 vol. 39 p. 10902 - 10910
LÓPEZ, E., DIVINS, N.J., ANZOLA, A., SCHBIB N.S., BORIO, D.O.
Ethanol steam reforming for hydrogen generation over structured catalysts
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY; Lugar: Amsterdam; Año: 2013 vol. 38 p. 4418 - 4428
CORNAGLIA C.A., ADROVER M.E., MÚNERA J.F., PEDERNERA M.N., BORIO D.O., LOMBARDO E.A.
Production of ultrapure hydrogen in a Pd-Ag membrane reactor using noble metal supported on La-Si oxides. Heterogeneous modeling for the water gas shift reaction
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY; Lugar: Amsterdam; Año: 2013
RODRIGUEZ M.L, PEDERNERA M.N., BORIO D.O.
Two-Dimensional modeling of a membrane reactor for ATR of methane
CATALYSIS TODAY; Lugar: Amsterdam; Año: 2012 vol. 193 p. 137 - 144
BRUSCHI Y., LÓPEZ, E.,SCHBIB, N.S., PEDERNERA, M.N., BORIO, D.O.
Theoretical study of the ethanol steam reforming in a parallel channel reactor
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY; Lugar: Amsterdam; Año: 2012 vol. 37 p. 14887 - 14894
M.L. RODRIGUEZ, D.E. ARDISSONE, E. LÓPEZ, M. N. PEDERNERA, D.O. BORIO
Reactor designs for ethylene production via ethane ODH: comparison of performance
INDUSTRIAL & ENGINEERING CHEMICAL RESEARCH; Año: 2011 vol. 50 p. 2690 - 2697
A. M. ANZOLA, Y. M. BRUSCHI, E. LÓPEZ, N. S. SCHBIB, M. N. PEDERNERA, D.O. BORIO
Heat supply and hydrogen yield in an ethanol micro-reformer
INDUSTRIAL & ENGINEERING CHEMICAL RESEARCH; Año: 2011 vol. 50 p. 2698 - 2705
M. E. ADROVER, A. ANZOLA, N. S. SCHBIB, M. N. PEDERNERA, D. O. BORIO
Effect of flow configuration on the behaviour of a membrane reactor operating without sweep gas
CATALYSIS TODAY; Año: 2010 vol. 156 p. 223 - 228
3. M.L. RODRIGUEZ, D.E. ARDISSONE, M. N. PEDERNERA, D.O. BORIO
Influence of the oxygen feed distribution on the performance of a catalytic reactor for ATR of methane
CATALYSIS TODAY; Año: 2010 vol. 156 p. 246 - 253
M. L. RODRIGUEZ, D. E. ARDISSONE, E. HERACLEOUS, A. A. LEMONIDOU, E. LÓPEZ, M. N. PEDERNERA, D. O. BORIO
Oxidative dehydrogenation of ethane to ethylene in a membrane reactor: a theoretical study
CATALYSIS TODAY; Año: 2010 vol. 157 p. 303 - 309
M.L. RODRIGUEZ, D.E. ARDISSONE, E. HERACLEOUS, A. A. LEMONIDOU, E. LÓPEZ, M. N. PEDERNERA, D.O. BORIO
Simulation of a membrane reactor for the catalytic oxydehydrogenation of ethane
INDUSTRIAL & ENGINEERING CHEMICAL RESEARCH; Año: 2009 vol. 48 p. 1090 - 1095
M. E. ADROVER, E. LÓPEZ, D. O. BORIO, M. N. PEDERNERA
Simulation of a membrane reactor for the water gas shift reaction: pressure and thermal effects
CHEMICAL ENGINEERING JOURNAL; Año: 2009 vol. 154 p. 196 - 202
M. E. ADROVER, E. LÓPEZ, D.O. BORIO, M. N. PEDERNERA
Theoretical study of a membrane reactor for the water gas shift reaction under non-isothermal conditions
AICHE JOURNAL; Año: 2009 vol. 55 p. 3206 - 3213
E. LÓPEZ, E. HERACLEOUS, A. A. LEMONIDOU, D. O. BORIO
Sudy of a multitubular fixed-bed reactor for ethylene production via ethane dehydrogenation
CHEMICAL ENGINEERING JOURNAL; Año: 2008 vol. 145 p. 308 - 315
TRUBIANO G.C.; BORIO D.O.; ERRAZU A.F.
Influence of the operating conditions and the external mass transfer limitations on the synthesis of fatty acid esters using a Candida antarctica lipase
ENZYME AND MICROBIAL TECHNOLOGY; Lugar: Amsterdam; Año: 2007 vol. 40 p. 716 - 722
M.N. PEDERNERA, J. PIÑA J., D.O. BORIO
Kinetic Evaluation of carbon formation in a membrane reactor for methane reforming
CHEMICAL ENGINEERING JOURNAL; Año: 2007 vol. 134 p. 138 - 144
M.E. ADROVER; E. LÓPEZ; D.O. BORIO; M. PEDERNERA
Heat effects in a membrane reactor for the water gas shift reaction
STUDIES IN SURFACE SCIENCE AND CATALYSIS; Lugar: Amsterdam; Año: 2007 vol. 167 p. 183 - 188
J. PIÑA; D. O. BORIO
Modeling and Simulation of an Autothermal Reformer
LATIN AMERICAN APPLIED RESEARCH; Lugar: Bahía Blanca, ARGENTINA; Año: 2006 vol. 36 p. 289 - 294
TRUBIANO G.C., BORIO D.O., FERREIRA M.L.
Ethyl Oleate Synthesis Using Candida rugosa Lipase in a Solvent Free System. Role of Hydrophobic Interactions.
BIOMACROMOLECULES; Lugar: Columbus, OH; Año: 2004 vol. 5 p. 1832 - 1840
PEDERNERA M.N., PIÑA J., BORIO D.O., BUCALÁ V.
Use of a heterogeneous two-dimensional model to improve the primary steam reformer performance
CHEMICAL ENGINEERING JOURNAL; Año: 2003 vol. 94 p. 29 - 40
C. GOMEZ, D.O. BORIO, N. S. SCHBIB
Simulation of an industrial packed-bed column for reactive absorption of CO2
LATIN AMERICAN APPLIED RESEARCH; Lugar: Bahía Blanca; Año: 2003 vol. 33 p. 201 - 205
15. J. PIÑA, V. BUCALÁ, D. O. BORIO
Optimization of steam reformers: heat-flux distribution and carbon formation
INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING; Año: 2003 vol. 1 p. 1 - 20
J. PIÑA, V. BUCALÁ AND D.O. BORIO
Influence of the Sulfur Poisoning on the Performance of a Primary Steam Reformer
INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING; Año: 2003 vol. 1 p. 1 - 20
PIÑA J., SCHBIB N.S., BUCALÁ V. ,BORIO D.O.
Influence of the Heat-Flux Profiles on the Operation of Primary Steam Reformers
INDUSTRIAL & ENGINEERING CHEMICAL RESEARCH; Año: 2001 vol. 40 p. 5215 - 5221
N. S. SCHBIB, M. PEDERNERA, D. O. BORIO
Dynamics and Control of a Radial-Flow Ammonia Synthesis Reactor
STUDIES IN SURFACE SCIENCE AND CATALYSIS; Año: 2001 vol. 133 p. 271 - 279
LÓPEZ, E., GÍGOLA C., BORIO D.O., BUCALÁ V.
Catalytic Combustion of Methane over Pd/Al2O3 in a Monolithic Reactor: Kinetic Study
STUDIES IN SURFACE SCIENCE AND CATALYSIS; Lugar: Amsterdam; Año: 2001 vol. 133 p. 625 - 630
MIGUEL V.U., TRUBIANO G.C., PÉREZ G., BORIO D.O., ERRAZU A.F.
Kinetic analysis of enzimatic esterification of fatty acids and ethanol
STUDIES IN SURFACE SCIENCE AND CATALYSIS; Lugar: Amsterdam; Año: 2001 vol. 133 p. 619 - 624
LOPEZ E., ERRAZU A.F., BORIO D.O., BUCALÁ V.
Alternative designs for a catalytic converter operating under autothermal conditions
CHEMICAL ENGINEERING SCIENCE; Año: 2000 vol. 55 p. 2143 - 2150
BORIO D.O., SCHBIB N.S., GATICA J.E.
Reversal flow in fixed-bed reactors operating under reaction-regeneration cycles
CHEMICAL ENGINEERING SCIENCE; Año: 1999 vol. 54 p. 1313 - 1318
SAVORETTI A.A., BORIO D.O., BUCALÁ V., PORRAS J.A:
Non-adiabatic radial-flow reactor for styrene production
CHEMICAL ENGINEERING SCIENCE; Año: 1999 vol. 54 p. 205 - 213
M. N. PEDERNERA, D. O. BORIO, N. S. SCHBIB,
Steady-state analysis and optimization of a radial-flow ammonia synthesis reactor
COMPUTERS AND CHEMICAL ENGINEERING; Año: 1999 vol. Supp p. 783 - 786
BORIO D.O., SCHBIB N.S., GATICA J.E.
Effect of catalyst deactivation on the dynamics of cyclic reactive processes
STUDIES IN SURFACE SCIENCE AND CATALYSIS; Lugar: Amsterdam; Año: 1999 vol. 122 p. 117 - 124
BUCALÁ V., BORIO D.O., PORRAS J.A.
Thermal Regimes in Cocurrently Cooled Fixed-bed reactors for parallel reactions: application to practical design problems
CHEMICAL ENGINEERING SCIENCE; Año: 1997 vol. 52 p. 1577 - 1587
PEDERNERA M.N., BORIO D.O., PORRAS J.A.
Steady-State Multiplicity in Cocurrently Cooled Autothermal Reactors
AICHE JOURNAL; Lugar: New York; Año: 1997 vol. 43 p. 127 - 134
PEDERNERA M.N., BORIO D.O., PORRAS J.A.
A new cocurrent reactor for ammonia synthesis
CHEMICAL ENGINEERING SCIENCE; Año: 1996 vol. 51 p. 2927 - 2932
D.O. BORIO, V. BUCALÁ, J. A. PORRAS
Thermal Regimes in Cocurrently Cooled Fixed-Bed Reactors
CHEMICAL ENGINEERING SCIENCE; Año: 1995 vol. 50 p. 3115 - 3123
BORIO D.O., SCHBIB N.S.
Simulation and optimization of a set of catalytic reactors used for dehydrogenation of butene into butadiene
COMPUTERS & INDUSTRIAL ENGINEERING; Año: 1995 vol. 19S p. 345 - 350
D. O. BORIO,; M. MENÉNDEZ; J. SANTAMARÍA
Simulation and Optimization of a Fixed Bed Reactor Operating in Coking-Regeneration Cycles
INDUSTRIAL & ENGINEERING CHEMICAL RESEARCH; Año: 1992 vol. 31 p. 2699 - 2707
BUCALÁ V., BORIO D.O., ROMAGNOLI J.A., PORRAS J.A.
Influence of Cooling Desing on Fixed-Bed Reactors Dynamics
AICHE JOURNAL; Lugar: New York; Año: 1992 vol. 38 p. 1990 - 1994
BORIO D.O., GATICA J.E., PORRAS J.A.
Wall-Cooled Fixed-Bed Reactors: Parametric Sensitivity as a Design Criterion
AICHE JOURNAL; Lugar: New York; Año: 1989 vol. 35 p. 287 - 292
BORIO D.O., BUCALÁ V., OREJAS J.A., PORRAS J.A.
Cocurrently-Cooled Fixed-Bed Reactors: A Simple Approach to Optimal Cooling Design
AICHE JOURNAL; Lugar: New York; Año: 1989 vol. 35 p. 1899 - 1902
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