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Prof. Miryan Cassanello
Universidad de Buenos Aires, Facultad de Ciencias Exactas y Naturales, Dep. Industrias

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Research Keywords & Expertise

0 Multiphase Flow
0 Advanced oxidation processes
0 Particle Tracking Velocimetry
0 catalytic processes
0 muliphase reactions

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Short Biography

Prof. Miryan Cassanello studied Chemistry at the University of Buenos Aires and obtained her PhD from the same university. After a postdoctoral stay at the École Polytechnique de Montréal, Canada, and later at the Washington University, St. Louis, Mo., USA, she returned to the University of Buenos Aires. Her research focuses mainly on multiphase reactors optimization and intensification, and applications to processes that turns residues into products or energy.

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Preprint
Published: 29 July 2021
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Currently, various industrial processes are carried out in fluidized bed reactors, such as fermentation, water treatment, and algae growth. Knowing its internal dynamics is fundamental for the intensification of these processes. This work assesses the motion of fluidized calcium alginate spheres under the influence of an upward fluid flow within a 1.2 m high and 0.1 m inner diameter acrylic column. The Radioactive Particle Tracking technique is a proper methodology to study the internal dynamics of these kinds of equipment. Liquid-Solid Fluidized Bed is compared with the Gas-Liquid-Solid Fluidized Bed operation mode in terms of mixing behavior. Data gathered is analyzed in view of Shannon entropy as a dynamic mixing measure. Mixing times are found to be of the same order of magnitude. However, the Liquid-Solid Fluidized Bed achieves a lower homogenization degree. Also, we found good agreement between two criteria for assessing stability for the mixed state: the Shannon Entropy time-series plateau and the Glansdorff-Prigogine criterion based on Fisher information.

ACS Style

Gabriel Salierno; Anton Gradišek; Mauricio Maestri; Julia Picabea; Miryan Cassanello; Cataldo De Blasio; María Angélica Cardona; Daniel Hojman; Héctor Somacal. Comparison of the Fluidized State Stability From Radioactive Particle Tracking Results Applied. 2021, 1 .

AMA Style

Gabriel Salierno, Anton Gradišek, Mauricio Maestri, Julia Picabea, Miryan Cassanello, Cataldo De Blasio, María Angélica Cardona, Daniel Hojman, Héctor Somacal. Comparison of the Fluidized State Stability From Radioactive Particle Tracking Results Applied. . 2021; ():1.

Chicago/Turabian Style

Gabriel Salierno; Anton Gradišek; Mauricio Maestri; Julia Picabea; Miryan Cassanello; Cataldo De Blasio; María Angélica Cardona; Daniel Hojman; Héctor Somacal. 2021. "Comparison of the Fluidized State Stability From Radioactive Particle Tracking Results Applied." , no. : 1.

Journal article
Published: 29 July 2021 in Chemical Engineering Research and Design
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The information obtained by one-dimensional Radioactive Particle Tracking is used to make an industrially relevant description of the macroscopic mixing of a three-phase bubble column. The objective is to characterize and compare the solid motion of granular activated carbon (dp = 1 mm) and calcium alginate beads (dp = 5 mm), widely used as adsorbents for pollutants and as support for catalysts, enzymes, and living organisms. The particles are suspended in water with upflowing air into a 0.1 m diameter and a 1 m height bubble column. The liquid–solid suspensions are in batch, and the air superficial velocity ranges within 0.01–0.12 m/s. The solid axial hold-up distribution of the carbon–water–air system is biased towards the bottom of the column, while the alginate–water–air system is more even. The axial dispersion coefficients obtained in both systems have a positive linear behavior within the operating range, which is uncannily marked in the carbon-water-air system, and it is an order of magnitude less than the alginate–water–air system. The contrasts of the two systems are mostly explained as a function of the solid densities. Axial mixing time distribution shows a sharp minimum at the second quartile of the column. Flow regime transition is assessed using information theory.

ACS Style

Gabriel Salierno; Mauricio Maestri; Julia Picabea; Miryan Cassanello; Cataldo De Blasio; María Angélica Cardona; Daniel Hojman; Héctor Somacal. Industrially relevant Radioactive Particle Tracking study on the motion of adsorbent granules suspended in a pilot-scale water–air three-phase fluidized bed. Chemical Engineering Research and Design 2021, 173, 305 -316.

AMA Style

Gabriel Salierno, Mauricio Maestri, Julia Picabea, Miryan Cassanello, Cataldo De Blasio, María Angélica Cardona, Daniel Hojman, Héctor Somacal. Industrially relevant Radioactive Particle Tracking study on the motion of adsorbent granules suspended in a pilot-scale water–air three-phase fluidized bed. Chemical Engineering Research and Design. 2021; 173 ():305-316.

Chicago/Turabian Style

Gabriel Salierno; Mauricio Maestri; Julia Picabea; Miryan Cassanello; Cataldo De Blasio; María Angélica Cardona; Daniel Hojman; Héctor Somacal. 2021. "Industrially relevant Radioactive Particle Tracking study on the motion of adsorbent granules suspended in a pilot-scale water–air three-phase fluidized bed." Chemical Engineering Research and Design 173, no. : 305-316.

Journal article
Published: 24 December 2020 in Heliyon
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Cattle concentrated animal feeding operations (feedlots), whose number has grown considerably in the last years, generate large volumes of wastewaters with a high organic load. The wastewaters are formed by rainfall-runoff of the accumulated manure and may contain hormones and antibiotics, which hampers the use of biological treatments. In this work, the feasibility of continuous separation of the suspended colloidal organic matter and nutrients to clarify the liquid and recover the solid is studied. A flocculation sedimentation system using a decentralized lamella settler is proposed, optimized and further tested in the field. Computational fluid dynamic (CFD) simulation is used to analyze the motion of the liquid and suspended inertial particles representing the formed flocs, for optimizing the settler. The simulations helped in the design of the bench-scale unit tested in the field. The clarified liquid was characterized to analyze its use for fertigation. The proposed treatment allowed excellent removal of organic matter (~98% chemical oxygen demand, and almost complete turbidity) and phosphorus (~95%). Organic nitrogen was partially removed (~70%) and ammonia nitrogen mostly remained in the liquid. Spectral characterization of the clarified liquid suggests that the remaining organic nitrogen is related to soluble protein-like compounds.

ACS Style

Santiago N. Fleite; Ana R. García; Christian De Los Santos; Leandro L. Missoni; Rocío Torres; M. Gabriela Lagorio; Miryan Cassanello. Simulation and optimization of a lamella settler for cattle feedlot wastewater treatment and nutrients recovery. Experimental validation in the field. Heliyon 2020, 6, e05840 .

AMA Style

Santiago N. Fleite, Ana R. García, Christian De Los Santos, Leandro L. Missoni, Rocío Torres, M. Gabriela Lagorio, Miryan Cassanello. Simulation and optimization of a lamella settler for cattle feedlot wastewater treatment and nutrients recovery. Experimental validation in the field. Heliyon. 2020; 6 (12):e05840.

Chicago/Turabian Style

Santiago N. Fleite; Ana R. García; Christian De Los Santos; Leandro L. Missoni; Rocío Torres; M. Gabriela Lagorio; Miryan Cassanello. 2020. "Simulation and optimization of a lamella settler for cattle feedlot wastewater treatment and nutrients recovery. Experimental validation in the field." Heliyon 6, no. 12: e05840.

Journal article
Published: 24 November 2020 in Energies
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Solid-liquid dissolution is a central step in many industrial applications such as pharmaceutical, process engineering, and pollution control. Accurate mathematical models are proposed to improve reactor design and process operations. Analytical methods are significantly beneficial in the case of iterative methods used within experimental investigations. In the present study, a detailed analytical solution for the general case of solid particles dissolving in multiphase chemical reaction systems is presented. In this model, the authors consider a formulation that considers the particles’ shape factor. The general case presented could be utilized within different problems of multiphase flows. These methods could be extended to different cases within the chemical engineering area. Examples are illustrated here in relation to limestone dissolution taking place within the Wet Flue Gas Desulfurization process, where calcium carbonate is dissolving in an acidic environment. The method is the most common used technology to abate SO2 released by fuel combustion. Limestone dissolution plays a major role in the process. Nevertheless, there is a need for improvements in the optimization of the WFGD process for scale-up purposes. The mathematical model has been tested by comparison with experimental data from several mild acidic dissolution assays of sedimentary and metamorphic limestone. We have found that R2 ⊂ 0.92 ± 0.06 from dozens of experiments. This fact verifies the model qualifications in capturing the main drivers of the system.

ACS Style

Cataldo De Blasio; Gabriel Salierno; Donatella Sinatra; Miryan Cassanello. Modeling of Limestone Dissolution for Flue Gas Desulfurization with Novel Implications. Energies 2020, 13, 6164 .

AMA Style

Cataldo De Blasio, Gabriel Salierno, Donatella Sinatra, Miryan Cassanello. Modeling of Limestone Dissolution for Flue Gas Desulfurization with Novel Implications. Energies. 2020; 13 (23):6164.

Chicago/Turabian Style

Cataldo De Blasio; Gabriel Salierno; Donatella Sinatra; Miryan Cassanello. 2020. "Modeling of Limestone Dissolution for Flue Gas Desulfurization with Novel Implications." Energies 13, no. 23: 6164.

Journal article
Published: 03 July 2019 in Chemical Engineering Science
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The current work focuses on the hydrodynamic study of liquid-solid mono and binary conical fluidized bed using the radioactive particle tracking technique. Two different sizes 0.6 and 1 mm diameter glass beads were used for the experiment. Two different bed compositions, mono dispersed (100 wt% of each solid) and 50 wt% mixture of the solids, were studied. A rich data base, including instantaneous velocities, mean and RMS velocities, granular temperature, etc., were calculated by suitable post-processing. Further, Hurst exponent, autocorrelation function, segregation index, Kolmogorov entropy, and correlation dimension were calculated using time series data to understand the mixing and chaotic nature of the fluidized bed for each set of data. Good degree of mixing was observed even at a low velocity of 0.07 m/s. Kolmogorov entropy and correlation dimension indicate regime change at liquid inlet velocity of 0.1 m/s for both mono and 50 wt% binary bed.

ACS Style

Lipika Kalo; Premkumar Kamalanathan; Harish J. Pant; Miryan C. Cassanello; Rajesh K. Upadhyay. Mixing and regime transition analysis of liquid-solid conical fluidized bed through RPT technique. Chemical Engineering Science 2019, 207, 702 -712.

AMA Style

Lipika Kalo, Premkumar Kamalanathan, Harish J. Pant, Miryan C. Cassanello, Rajesh K. Upadhyay. Mixing and regime transition analysis of liquid-solid conical fluidized bed through RPT technique. Chemical Engineering Science. 2019; 207 ():702-712.

Chicago/Turabian Style

Lipika Kalo; Premkumar Kamalanathan; Harish J. Pant; Miryan C. Cassanello; Rajesh K. Upadhyay. 2019. "Mixing and regime transition analysis of liquid-solid conical fluidized bed through RPT technique." Chemical Engineering Science 207, no. : 702-712.

Research article
Published: 19 June 2019 in Industrial & Engineering Chemistry Research
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There has been a growing interest in the last decades to technologies that transform biomass-derived feedstock into renewable chemicals. A group of target molecules derived from biomass as key intermediates between raw materials and final products have been designed as “platform chemicals”. Sustainable processes involve the use of renewable feedstock, but also pursue low energy consumption, the use of less hazardous materials and diminished generation of waste. This review aims to present recent advances on environmentally friendly catalytic oxidation routes for transforming three platform chemicals, ethanol, glycerol and 5-hydroxymethylfurfural, to value added intermediates and final products using air or oxygen as oxidants, water without additives (base-free) as solvent, and preferably under moderate operating conditions. Works carried out under continuous flow have been particularly reviewed.

ACS Style

María Alejandra Ayude; Lucila Doumic; Miryan Celeste Cassanello; Krishna D. P. Nigam. Clean Catalytic Oxidation for Derivatization of Key Biobased Platform Chemicals: Ethanol, Glycerol, and Hydroxymethyl Furfural. Industrial & Engineering Chemistry Research 2019, 58, 16077 -16095.

AMA Style

María Alejandra Ayude, Lucila Doumic, Miryan Celeste Cassanello, Krishna D. P. Nigam. Clean Catalytic Oxidation for Derivatization of Key Biobased Platform Chemicals: Ethanol, Glycerol, and Hydroxymethyl Furfural. Industrial & Engineering Chemistry Research. 2019; 58 (35):16077-16095.

Chicago/Turabian Style

María Alejandra Ayude; Lucila Doumic; Miryan Celeste Cassanello; Krishna D. P. Nigam. 2019. "Clean Catalytic Oxidation for Derivatization of Key Biobased Platform Chemicals: Ethanol, Glycerol, and Hydroxymethyl Furfural." Industrial & Engineering Chemistry Research 58, no. 35: 16077-16095.

Journal article
Published: 14 February 2019 in Journal of Environmental Management
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A novel hierarchically structured composite aimed as a stable catalyst for the heterogeneous Fenton-type (HFT) oxidation process was developed by using a cost-effective and versatile technique. Prussian Blue nanoparticles (PBNP) were dispersed onto aligned macroporous TiO2 (rutile) monoliths prepared via directional freezing of aqueous dispersions of TiO2 nanoparticles. The catalytic performance was evaluated in the HFT oxidation of an azo dye frequently used as a model contaminant, Orange G (OG). Experiments were carried out in a liquid batch-recycle reactor, in which the liquid flow rate was set to ensure negligible external mass transfer resistance. The catalyst exhibited good activity to form highly oxidative radicals from hydrogen peroxide decomposition, which readily discolored OG. Significant reduction of the time required to attain complete discoloration and improvement in TOC removal were achieved by adjusting operating conditions and oxidant dosage strategies. Almost complete OG conversion at around 90 min and 34.4% of TOC removal after 4 h were achieved by using the best evaluated strategy. The catalyst activity was tested under specific operating conditions and remained unaltered during 42 cycles of 4 h each (total 168 h). The fresh and used PBNP/TiO2 catalysts and the support were thoroughly characterized by several techniques. Results supported the excellent stability exhibited by the catalyst in the OG HFT oxidation.

ACS Style

Lucila Doumic; Micaela Génova; Gregor Žerjav; Albin Pintar; Miryan C. Cassanello; Hernán E. Romeo; María A. Ayude. Hierarchically structured TiO2-based composites for Fenton-type oxidation processes. Journal of Environmental Management 2019, 236, 591 -602.

AMA Style

Lucila Doumic, Micaela Génova, Gregor Žerjav, Albin Pintar, Miryan C. Cassanello, Hernán E. Romeo, María A. Ayude. Hierarchically structured TiO2-based composites for Fenton-type oxidation processes. Journal of Environmental Management. 2019; 236 ():591-602.

Chicago/Turabian Style

Lucila Doumic; Micaela Génova; Gregor Žerjav; Albin Pintar; Miryan C. Cassanello; Hernán E. Romeo; María A. Ayude. 2019. "Hierarchically structured TiO2-based composites for Fenton-type oxidation processes." Journal of Environmental Management 236, no. : 591-602.

Journal article
Published: 08 November 2018 in Chemical Engineering Journal
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The motion of calcium alginate spheres in a liquid-solid fluidized bed is examined by radioactive particle tracking (RPT) and simulated by computational fluid dynamics coupled with discrete element method (CFD-DEM). Observables relevant for phenomenological models of the solid motion determined from RPT are compared with those arising from the CFD-DEM simulations. Bed expansion, solid distribution, time averaged velocity fields and axial dispersion coefficients calculated from simulations reasonably agree with the experimental values. The influence of the liquid inlet distribution on simulations results is examined. A non-negligible effect is observed on the predicted velocity profiles, solid distribution and dispersion coefficients, mainly in the entrance region. Uniform liquid distribution at the entrance generally predicts a less steeped profile. When the liquid inlet distribution is parameterized considering the geometry of the experimental distributor, the fitting of the solid mean axial velocity and solid distribution radial profiles, judged from a sum of squares of relative errors, improves in 90% and 80%, respectively, compared to results obtained when considering a uniform liquid distribution at the entrance.

ACS Style

Mauricio Maestri; Gabriel Salierno; Stella Piovano; Miryan Cassanello; María Angélica Cardona; Daniel Hojman; Héctor Somacal. CFD-DEM modeling of solid motion in a water-calcium alginate fluidized column and its comparison with results from radioactive particle tracking. Chemical Engineering Journal 2018, 377, 120339 .

AMA Style

Mauricio Maestri, Gabriel Salierno, Stella Piovano, Miryan Cassanello, María Angélica Cardona, Daniel Hojman, Héctor Somacal. CFD-DEM modeling of solid motion in a water-calcium alginate fluidized column and its comparison with results from radioactive particle tracking. Chemical Engineering Journal. 2018; 377 ():120339.

Chicago/Turabian Style

Mauricio Maestri; Gabriel Salierno; Stella Piovano; Miryan Cassanello; María Angélica Cardona; Daniel Hojman; Héctor Somacal. 2018. "CFD-DEM modeling of solid motion in a water-calcium alginate fluidized column and its comparison with results from radioactive particle tracking." Chemical Engineering Journal 377, no. : 120339.

Journal article
Published: 01 September 2018 in Chemical Engineering Journal
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In current work, the radioactive particle tracking (RPT) technique has been used to investigate the behavior of gas-solid conical mono and binary fluidized bed. The dynamics of the bed has been analyzed using both time-averaged and fluctuation quantities at different gas inlet velocities and bed compositions. The binary bed was composed of glass beads of two different diameters 1 mm and 0.6 mm. The bed of 0:100, 50:50 and 100:0 by wt % of both the particles were investigated. Time-averaged quantities like mean axial velocities, RMS velocities, and granular temperature indicate that behavior of conical bed at the top and bottom sections are significantly different. Gas-solid interactions mainly dominate the bottom section while particle-particle interaction plays a critical role at the top section. Further, time series and chaos analysis of RPT data were performed. Hurst exponent, autocorrelation coefficient, and mixing index were calculated through time series analysis. The results indicate that better mixing is observed in conical bed even at low velocity compared to cylindrical fluidized-bed. It also reveals a regime transition around 5.7 m/s gas inlet velocity. Finally, Kolmogorov entropy and correlation dimension calculated through chaos analysis of RPT data confirm flow regime transition at gas inlet velocity around 5.7 m/s, for all the examined bed compositions.

ACS Style

Lipika Kalo; Harish J. Pant; Miryan C. Cassanello; Rajesh K. Upadhyay. Time series analysis of a binary gas-solid conical fluidized bed using radioactive particle tracking (RPT) technique data. Chemical Engineering Journal 2018, 377, 119807 .

AMA Style

Lipika Kalo, Harish J. Pant, Miryan C. Cassanello, Rajesh K. Upadhyay. Time series analysis of a binary gas-solid conical fluidized bed using radioactive particle tracking (RPT) technique data. Chemical Engineering Journal. 2018; 377 ():119807.

Chicago/Turabian Style

Lipika Kalo; Harish J. Pant; Miryan C. Cassanello; Rajesh K. Upadhyay. 2018. "Time series analysis of a binary gas-solid conical fluidized bed using radioactive particle tracking (RPT) technique data." Chemical Engineering Journal 377, no. : 119807.

Journal article
Published: 01 August 2018 in Flow Measurement and Instrumentation
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ACS Style

Gabriel Salierno; Mauricio Maestri; Stella Piovano; Miryan Cassanello; María Angélica Cardona; Daniel Hojman; Héctor Somacal. Solid motion in a three-phase bubble column examined with Radioactive Particle Tracking. Flow Measurement and Instrumentation 2018, 62, 196 -204.

AMA Style

Gabriel Salierno, Mauricio Maestri, Stella Piovano, Miryan Cassanello, María Angélica Cardona, Daniel Hojman, Héctor Somacal. Solid motion in a three-phase bubble column examined with Radioactive Particle Tracking. Flow Measurement and Instrumentation. 2018; 62 ():196-204.

Chicago/Turabian Style

Gabriel Salierno; Mauricio Maestri; Stella Piovano; Miryan Cassanello; María Angélica Cardona; Daniel Hojman; Héctor Somacal. 2018. "Solid motion in a three-phase bubble column examined with Radioactive Particle Tracking." Flow Measurement and Instrumentation 62, no. : 196-204.

Journal article
Published: 01 June 2018 in Chinese Journal of Chemical Engineering
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ACS Style

Gabriel Salierno; Mauricio Maestri; Stella Piovano; Miryan Cassanello; María Angélica Cardona; Daniel Hojman; Héctor Somacal. Features of the motion of gel particles in a three-phase bubble column under foaming and non-foaming conditions. Chinese Journal of Chemical Engineering 2018, 26, 1370 -1382.

AMA Style

Gabriel Salierno, Mauricio Maestri, Stella Piovano, Miryan Cassanello, María Angélica Cardona, Daniel Hojman, Héctor Somacal. Features of the motion of gel particles in a three-phase bubble column under foaming and non-foaming conditions. Chinese Journal of Chemical Engineering. 2018; 26 (6):1370-1382.

Chicago/Turabian Style

Gabriel Salierno; Mauricio Maestri; Stella Piovano; Miryan Cassanello; María Angélica Cardona; Daniel Hojman; Héctor Somacal. 2018. "Features of the motion of gel particles in a three-phase bubble column under foaming and non-foaming conditions." Chinese Journal of Chemical Engineering 26, no. 6: 1370-1382.

Journal article
Published: 01 September 2017 in Chemical Engineering Journal
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ACS Style

Gabriel Salierno; Mauricio Maestri; Stella Piovano; Miryan Cassanello; María Angélica Cardona; Daniel Hojman; Héctor Somacal. Calcium alginate beads motion in a foaming three-phase bubble column. Chemical Engineering Journal 2017, 324, 358 -369.

AMA Style

Gabriel Salierno, Mauricio Maestri, Stella Piovano, Miryan Cassanello, María Angélica Cardona, Daniel Hojman, Héctor Somacal. Calcium alginate beads motion in a foaming three-phase bubble column. Chemical Engineering Journal. 2017; 324 ():358-369.

Chicago/Turabian Style

Gabriel Salierno; Mauricio Maestri; Stella Piovano; Miryan Cassanello; María Angélica Cardona; Daniel Hojman; Héctor Somacal. 2017. "Calcium alginate beads motion in a foaming three-phase bubble column." Chemical Engineering Journal 324, no. : 358-369.

Journal article
Published: 03 May 2016 in RSC Advances
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The influence of the synthesis procedure of supported Prussian blue nanoparticles (PBNP) on their activity and stability as a Fenton-type catalyst is studied.

ACS Style

Lucila Doumic; Gabriel Salierno; Cinthia Paula Ramos; Patricia M. Haure; Miryan Cassanello; Maria Alejandra Ayude. “Soluble” vs. “insoluble” Prussian blue based catalysts: influence on Fenton-type treatment. RSC Advances 2016, 6, 46625 -46633.

AMA Style

Lucila Doumic, Gabriel Salierno, Cinthia Paula Ramos, Patricia M. Haure, Miryan Cassanello, Maria Alejandra Ayude. “Soluble” vs. “insoluble” Prussian blue based catalysts: influence on Fenton-type treatment. RSC Advances. 2016; 6 (52):46625-46633.

Chicago/Turabian Style

Lucila Doumic; Gabriel Salierno; Cinthia Paula Ramos; Patricia M. Haure; Miryan Cassanello; Maria Alejandra Ayude. 2016. "“Soluble” vs. “insoluble” Prussian blue based catalysts: influence on Fenton-type treatment." RSC Advances 6, no. 52: 46625-46633.

Journal article
Published: 01 October 2015 in Chemical Engineering Journal
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ACS Style

Lucila Doumic; Petrick Soares; Maria Alejandra Ayude; Miryan Cassanello; Rui Boaventura; Vítor Vilar. Enhancement of a solar photo-Fenton reaction by using ferrioxalate complexes for the treatment of a synthetic cotton-textile dyeing wastewater. Chemical Engineering Journal 2015, 277, 86 -96.

AMA Style

Lucila Doumic, Petrick Soares, Maria Alejandra Ayude, Miryan Cassanello, Rui Boaventura, Vítor Vilar. Enhancement of a solar photo-Fenton reaction by using ferrioxalate complexes for the treatment of a synthetic cotton-textile dyeing wastewater. Chemical Engineering Journal. 2015; 277 ():86-96.

Chicago/Turabian Style

Lucila Doumic; Petrick Soares; Maria Alejandra Ayude; Miryan Cassanello; Rui Boaventura; Vítor Vilar. 2015. "Enhancement of a solar photo-Fenton reaction by using ferrioxalate complexes for the treatment of a synthetic cotton-textile dyeing wastewater." Chemical Engineering Journal 277, no. : 86-96.

Journal article
Published: 01 February 2015 in Catalysis Today
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ACS Style

Lucila Doumic; G. Salierno; M. Cassanello; P. Haure; M. Ayude. Efficient removal of Orange G using Prussian Blue nanoparticles supported over alumina. Catalysis Today 2015, 240, 67 -72.

AMA Style

Lucila Doumic, G. Salierno, M. Cassanello, P. Haure, M. Ayude. Efficient removal of Orange G using Prussian Blue nanoparticles supported over alumina. Catalysis Today. 2015; 240 ():67-72.

Chicago/Turabian Style

Lucila Doumic; G. Salierno; M. Cassanello; P. Haure; M. Ayude. 2015. "Efficient removal of Orange G using Prussian Blue nanoparticles supported over alumina." Catalysis Today 240, no. : 67-72.

Journal article
Published: 21 January 2015 in Chemical Engineering & Technology
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The inclusion of a structured packing as internal in a liquid‐solid fluidized bed allows expansion of the liquid velocity operation range before elutriation, promoting the liquid solid contact and mixing. The bed expansion of liquid‐solid fluidized beds provided with structured packing as internals is examined, for solids denser than the liquid phase and within a wide range of operating conditions. A correlation to estimate the bed expansion in liquid‐solid fluidized beds using structured packing as internals is developed. In addition, the feasibility of employing structured packing as internals for favoring classification of different density particles is demonstrated by analyzing the mass elutriated from the column at different liquid velocities for single particles or binary mixtures.

ACS Style

Stella Piovano; Gabriel L. Salierno; Emiliano Montmany; Mauro D'agostino; Mauricio Maestri; Miryan Cassanello. Bed Expansion and Particle Classification in Liquid Fluidized Beds with Structured Internals. Chemical Engineering & Technology 2015, 38, 423 -430.

AMA Style

Stella Piovano, Gabriel L. Salierno, Emiliano Montmany, Mauro D'agostino, Mauricio Maestri, Miryan Cassanello. Bed Expansion and Particle Classification in Liquid Fluidized Beds with Structured Internals. Chemical Engineering & Technology. 2015; 38 (3):423-430.

Chicago/Turabian Style

Stella Piovano; Gabriel L. Salierno; Emiliano Montmany; Mauro D'agostino; Mauricio Maestri; Miryan Cassanello. 2015. "Bed Expansion and Particle Classification in Liquid Fluidized Beds with Structured Internals." Chemical Engineering & Technology 38, no. 3: 423-430.

Conference paper
Published: 27 October 2014 in All Days
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A new automatic fault diagnostic method based on variable trend analysis was developed. Every time a fault is detected, the proposed method uses a local model to determine the variable trends associated to the detected fault. The fault identification is achieved by comparing the extracted variable trends with a previously generated library of faults signatures. The method was implemented and tested with a set of faults purposedly generated in an oil production well equipped with a pressure cavity pump (PCP). It was able to correctly identify all the generated faults, outperforming simpler versions of the method based on global models.

ACS Style

Gabriel Horowitz; Edgardo Ariel Faundez; Mauricio Maestri; Miryan Cassanello. Fault Diagnosis in Oil Wells. All Days 2014, 1 .

AMA Style

Gabriel Horowitz, Edgardo Ariel Faundez, Mauricio Maestri, Miryan Cassanello. Fault Diagnosis in Oil Wells. All Days. 2014; ():1.

Chicago/Turabian Style

Gabriel Horowitz; Edgardo Ariel Faundez; Mauricio Maestri; Miryan Cassanello. 2014. "Fault Diagnosis in Oil Wells." All Days , no. : 1.

Journal article
Published: 01 May 2014 in Computers & Chemical Engineering
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ACS Style

Mauricio Maestri; Daniel Ziella; Miryan Cassanello; Gabriel Horowitz. Automatic qualitative trend simulation method for diagnosing faults in industrial processes. Computers & Chemical Engineering 2014, 64, 55 -62.

AMA Style

Mauricio Maestri, Daniel Ziella, Miryan Cassanello, Gabriel Horowitz. Automatic qualitative trend simulation method for diagnosing faults in industrial processes. Computers & Chemical Engineering. 2014; 64 ():55-62.

Chicago/Turabian Style

Mauricio Maestri; Daniel Ziella; Miryan Cassanello; Gabriel Horowitz. 2014. "Automatic qualitative trend simulation method for diagnosing faults in industrial processes." Computers & Chemical Engineering 64, no. : 55-62.

Journal article
Published: 01 October 2013 in Applied Catalysis B: Environmental
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ACS Style

Lucila I. Doumic; Patricia M. Haure; Miryan Cassanello; Maria Alejandra Ayude. Mineralization and efficiency in the homogeneous Fenton Orange G oxidation. Applied Catalysis B: Environmental 2013, 142-143, 214 -221.

AMA Style

Lucila I. Doumic, Patricia M. Haure, Miryan Cassanello, Maria Alejandra Ayude. Mineralization and efficiency in the homogeneous Fenton Orange G oxidation. Applied Catalysis B: Environmental. 2013; 142-143 ():214-221.

Chicago/Turabian Style

Lucila I. Doumic; Patricia M. Haure; Miryan Cassanello; Maria Alejandra Ayude. 2013. "Mineralization and efficiency in the homogeneous Fenton Orange G oxidation." Applied Catalysis B: Environmental 142-143, no. : 214-221.

Journal article
Published: 01 August 2013 in Chemical Engineering Science
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ACS Style

Gabriel L. Salierno; Mauricio Maestri; Stella Piovano; Miryan Cassanello; María Angélica Cardona; Daniel Hojman; Héctor Somacal. Discrete axial motion of a radioactive tracer reconstructed from the response of axially aligned detectors: Application to the analysis of a bubble column dynamics. Chemical Engineering Science 2013, 100, 402 -412.

AMA Style

Gabriel L. Salierno, Mauricio Maestri, Stella Piovano, Miryan Cassanello, María Angélica Cardona, Daniel Hojman, Héctor Somacal. Discrete axial motion of a radioactive tracer reconstructed from the response of axially aligned detectors: Application to the analysis of a bubble column dynamics. Chemical Engineering Science. 2013; 100 ():402-412.

Chicago/Turabian Style

Gabriel L. Salierno; Mauricio Maestri; Stella Piovano; Miryan Cassanello; María Angélica Cardona; Daniel Hojman; Héctor Somacal. 2013. "Discrete axial motion of a radioactive tracer reconstructed from the response of axially aligned detectors: Application to the analysis of a bubble column dynamics." Chemical Engineering Science 100, no. : 402-412.