Listar FRRo - I+D+i - Artículos en Revistas por autor "Mussati, Miguel Ceferino"
Mostrando ítems 1-7 de 7
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Cost-based comparison between membrane systems and chemical absorption processes for CO2 capture from flue gas.
Arias, Ana Marisa; Mores, Patricia Liliana; Scenna, Nicolás José; Caballero, José Antonio; Mussati, Miguel Ceferino; Mussati, Sergio Fabián; 0000-0002-6716-6633; 0000-0001-6026-142X; 0000-0002-1129-8725; 0000-0002-6104-5179; 0000-0002-4132-0292 (2019-05-09)An optimization study of membrane-based separation systems for carbon dioxide capture from flue gas of power plants is conducted, considering the possibility of employing up to four stages and using diverse options to ... -
Development of extrinsic functions for optimal synthesis and design : application to distillation-based separation processes.
Manassaldi, Juan Ignacio; Mussati, Miguel Ceferino; Scenna, Nicolás José; Mussati, Sergio Fabián; 0009-0003-4386-4167; 0000-0002-6104-5179; 0000-0002-1129-8725; 0000-0002-4132-0292 (2019-04-09)This work deals with the development and implementation of mathematical models in the General Algebraic Modeling System (GAMS) environment for optimization purposes, involving extrinsic functions that are executed outside ... -
Membrane-based processes: optimization of hydrogen separation by minimization of power, membrane area, and cost.
Mores, Patricia Liliana; Arias, Ana Marisa; Scenna, Nicolás José; Caballero, José Antonio; Mussati, Sergio Fabián; Mussati, Miguel Ceferino; 0000-0001-6026-142X; 0000-0002-6716-6633; 0000-0002-1129-8725; 0000-0001-6470-2907; 0000-0002-4132-0292; 0000-0002-6104-5179 (2018-11-12)This work deals with the optimization of two-stage membrane systems for H2 separation from off-gases in hydrocarbons processing plants to simultaneously attain high values of both H2 recovery and H2 product purity. First, ... -
Optimal design of a two-stage membrane system for hydrogen separation in refining processes.
Arias, Ana Marisa; Mores, Patricia Liliana; Scenna, Nicolás José; Caballero, José Antonio; Mussati, Sergio Fabián; Mussati, Miguel Ceferino; 0000-0002-6716-6633; 0000-0001-6026-142X; 0000-0002-1129-8725; 0000-0001-6470-2907; 0000-0002-4132-0292; 0000-0002-6104-5179 (2018-10-31)This paper fits into the process system engineering field by addressing the optimization of a two-stage membrane system for H2 separation in refinery processes. To this end, a nonlinear mathematical programming (NLP) ... -
Optimization of the design, operating conditions, and coupling configuration of combined cycle power plants and CO2 capture processes by minimizing the mitigation cost.
Mores, Patricia Liliana; Manassaldi, Juan Ignacio; Scenna, Nicolás José; Caballero, José Antonio; Mussati, Miguel Ceferino; Mussati, Sergio Fabián; 0000-0001-6026-142X; 0009-0003-4386-4167; 0000-0002-1129-8725; 0000-0001-6470-2907; 0000-0002-6104-5179; 0000-0002-4132-0292 (2017-10-04)This paper deals with the optimization of the coupling between a natural gas combined cycle (NGCC plant and a post-combustion CO2 capture process by minimizing the mitigation cost – defined as the ratio between the cost ... -
Optimization of triple-pressure combined-cycle power plants by generalized disjunctive programming and extrinsic functions.
Manassaldi, Juan Ignacio; Mussati, Miguel Ceferino; Scenna, Nicolás José; Mussati, Sergio Fabián; 0009-0003-4386-4167; 0000-0002-6104-5179; 0000-0002-1129-8725; 0000-0002-4132-0292 (2021-02-01)A new mathematical framework for optimal synthesis, design, and operation of triple-pressure steamreheat combined-cycle power plants (CCPP) is presented. A superstructure-based representation of the process, which embeds ... -
Process optimization and revamping of combined-cycle heat and power plants integrated with thermal desalination processes.
Manassaldi, Juan Ignacio; Mussati, Miguel Ceferino; Scenna, Nicolás José; Morosuk, Tatiana; Mussati, Sergio Fabián; 0009-0003-4386-4167; 0000-0002-6104-5179; 0000-0002-1129-8725; 0000-0003-2968-4293; 0000-0002-4132-0292 (2021-06-06)Optimal revamping, sizing, and operation of an existing gas-turbine combined-cycle dual-purpose power/desalination plant – simultaneous electricity and freshwater generation – which operates with a heat recovery steam ...