| 1 |
Nonlinear Model for the Globally Optimal Design of Vertical Vapor Liquid Separation Vessels
Fischer CD, Costa ALH, Bagajewicz MJ
Industrial & Engineering Chemistry Research, 59(48), 21155, 2020 |
| 2 |
Hydrogen and energy savings using heuristic allocation of mass exchangers in process synthesis: Technical analysis
Fischer CD, Iribarren OA
International Journal of Hydrogen Energy, 44(26), 13509, 2019 |
| 3 |
Oxygen integration of autothermal reforming of ethanol with oxygen production, through ion transport membranes in countercurrent configuration
Fischer CD, Iribarren OA
Computers & Chemical Engineering, 99, 245, 2017 |
| 4 |
Oxygen integration between a gasification process and oxygen production using a mass exchange heuristic
Fischer CD, Iribarren OA
International Journal of Hydrogen Energy, 41(4), 2399, 2016 |
| 5 |
Hydrogen recovery from the purge stream of a cyclohexane production process using a mass exchange heuristic
Fischer CD, Iribarren OA
International Journal of Hydrogen Energy, 39(35), 20094, 2014 |
| 6 |
Improvements in the Design of the Cyclohexane Production Process Implementing Mass Exchange with a Counter Current Gas Permeation Membrane
Fischer CD, Iribarren OA
Industrial & Engineering Chemistry Research, 52(4), 1698, 2013 |
| 7 |
Hydrogen recovery from the purge stream of an HDA process using the concept of Mass Exchange Networks
Fischer CD, Iribarren OA
International Journal of Hydrogen Energy, 38(15), 6381, 2013 |
| 8 |
Improvements in the Design of the Ammonia Synthesis Process Implementing Counter Current Gas Permeation Modules
Fischer CD, Iribarren OA
Industrial & Engineering Chemistry Research, 51(50), 16410, 2012 |
| 9 |
Synthesis of a Mass Integrated Biodiesel Process
Fischer CD, Iribarren OA
Industrial & Engineering Chemistry Research, 50(11), 6849, 2011 |
| 10 |
Mass Integration as a Design Heuristic: Improvements in the HDA Process
Fischer CD, Iribarren OA
Industrial & Engineering Chemistry Research, 50(22), 12664, 2011 |
