1 |
Minimizing the total cost of multi effect evaporation systems for seawater desalination Druetta P, Aguirre P, Mussati S Desalination, 344, 431, 2014 |
2 |
Optimization of Multi-Effect Evaporation desalination plants Druetta P, Aguirre P, Mussati S Desalination, 311, 1, 2013 |
3 |
CO2 capture using monoethanolamine (MEA) aqueous solution: Modeling and optimization of the solvent regeneration and CO2 desorption process Mores P, Scenna N, Mussati S Energy, 45(1), 1042, 2012 |
4 |
Post-combustion CO2 capture process: Equilibrium stage mathematical model of the chemical absorption of CO2 into monoethanolamine (MEA) aqueous solution Mores P, Scenna N, Mussati S Chemical Engineering Research & Design, 89(9A), 1587, 2011 |
5 |
Optimization of post-combustion CO2 process using DEA-MDEA mixtures Rodriguez N, Mussati S, Scenna N Chemical Engineering Research & Design, 89(9A), 1763, 2011 |
6 |
Influence of product composition and operating conditions on the unsteady behavior of hard candy cooling process Reinheimer MA, Mussati S, Scenna NJ Journal of Food Engineering, 101(4), 409, 2010 |
7 |
MSF design taken into account availability Scenna N, Mussati S Desalination, 222(1-3), 673, 2008 |
8 |
Dual-purpose desalination plants. Part I. Optimal design Mussati S, Aguirre P, Scenna N Desalination, 153(1-3), 179, 2003 |
9 |
Dual-purpose desalination plants. Part II. Optimal configuration Mussati S, Aguirre P, Scenna N Desalination, 153(1-3), 185, 2003 |
10 |
Optimal MSF plant design Mussati S, Pio A, Scenna NJ Desalination, 138(1-3), 341, 2001 |