References
- Araújo AB, Brito RP, Vasconcelos LS. 2007. Exergetic analysis of distillation processes—A case study. Energy. 32(7):1185–1193. doi:https://doi.org/10.1016/j.energy.2006.07.003
- Bandyopadhyay S. 2007. Thermal integration of a distillation column through side-exchangers. Chem Eng Res Des. 85(1):155–166. doi:https://doi.org/10.1205/cherd06108R1
- Battisti R, Claumann CA, Marangoni C, Machado RAF. 2019. Optimization of pressure-swing distillation for anhydrous ethanol purification by the simulated annealing algorithm. Braz J Chem Eng. 36(1):453–469. doi:https://doi.org/10.1590/0104-6632.20190361s20180133
- Battisti R, Machado RAF, Marangoni C. 2020a. A background review on falling film distillation in wetted-wall columns: from fundamentals towards intensified technologies. Chem Eng Process - Process Intensif. 150(C):107873. doi:https://doi.org/10.1016/j.cep.2020.107873
- Battisti R, Claumann CA, Manenti F, Machado RAF, Marangoni C. 2020b. Dynamic modeling with experimental validation and control of a two-phase closed thermosyphon as heat supplier of a novel pilot-scale falling film distillation unit. Comput Chem Eng. 143:107078. doi:https://doi.org/10.1016/j.compchemeng.2020.107078
- Battisti R, Milanez KW, Mantelli MBH, dos Santos MC, Medina LC, Marangoni C, Machado RAF. 2020c. Energy conditions assessment of a two-phase annular thermosyphon used as heat supplier for a new pilot-scale falling film distillation unit. Therm Sci Eng Prog. 19:100648. doi:https://doi.org/10.1016/j.tsep.2020.100648
- Battisti R, Claumann CA, Manenti F, Machado RAF, Marangoni C. 2021. Machine learning modeling and genetic algorithm-based optimization of a novel pilot-scale thermosyphon-assisted falling film distillation unit. Sep Purif Technol. 259:118122. doi:https://doi.org/10.1016/j.seppur.2020.118122
- Blahušiak M, Kiss AA, Kersten SRA, Schuur B. 2016. Quick assessment of binary distillation efficiency using a heat engine perspective. Energy. 116:20–31. doi:https://doi.org/10.1016/j.energy.2016.09.097
- Bradtmöller C, Scholl S. 2015. Geometry and viscosity effects on separation efficiency in distillation. Chem Eng Res Des. 99:75–86. doi:https://doi.org/10.1016/j.cherd.2015.03.013
- Cerda J, Westerberg AW. 1981. Shortcut methods for complex distillation columns. 1. Minimum reflux. Ind Eng Chem Proc Des Dev. 20(3):546–557. doi:https://doi.org/10.1021/i200014a028
- da Silva AK, Mantelli MBH. 2004. Thermal applicability of two-phase thermosyphons in cooking chambers––experimental and theoretical analysis. Appl Therm Eng. 24(5-6):717–733. doi:https://doi.org/10.1016/j.applthermaleng.2003.09.013
- Dantas TNC, Cabral TJO, Neto AAD, Moura MCPA. 2020. Enrichmnent of patchoulol extracted from patchouli (Pogostemon cablin) oil by molecular distillation using response surface and artificial neural network models. J Ind Eng Chem. 81:219–227. doi:https://doi.org/10.1016/j.jiec.2019.09.011
- Dejanovic I, Matijasevic L, Olujic Z. 2010. Dividing wall column - A breakthrough towards sustainable distilling. Chem Eng Process Process Intensif. 49(6):559–580. doi:https://doi.org/10.1016/j.cep.2010.04.001
- Ferrandi C, Iorizzo F, Mameli M, Zinna S, Marengo M. 2013. Lumped parameter model of sintered heat pipe: transient numerical analysis and validation. Appl Therm Eng. 50(1):1280–1290. doi:https://doi.org/10.1016/j.applthermaleng.2012.07.022
- Huang K, Wang S-J, Shan L, Zhu Q, Qian J. 2007. Seeking synergistic effect—A key principle in process intensification. Sep Purif Technol. 57(1):111–120. doi:https://doi.org/10.1016/j.seppur.2007.03.022
- Jana AK. 2017. An energy efficient middle vessel batch distillation: techno-economic feasibility, dynamics and control. Appl Therm Eng. 123:411–421. doi:https://doi.org/10.1016/j.applthermaleng.2017.05.106
- Jouhara H, Chauhan A, Nannou T, Almahmoud S, Delpech B, Wrobel LC. 2017. Heat pipe based systems - Advances and applications. Energy. 128:729–754. doi:https://doi.org/10.1016/j.energy.2017.04.028
- Kiran B, Jana AK. 2016. Thermal integration of vapor recompression in a heat-integrated distillation: impact of multiple intermediate reboilers. Chem Eng Res Des. 114:171–179. doi:https://doi.org/10.1016/j.cherd.2016.08.021
- Kiss AA. 2014. Distillation technology – still young and full of breakthrough opportunities. J Chem Technol Biotechnol. 89(4):479–498. doi:https://doi.org/10.1002/jctb.4262
- Kiss AA, Olujic Ž. 2014. A review on process intensification in internally heat-integrated distillation columns. Chem Eng Process Process Intensif. 86:125–144. doi:https://doi.org/10.1016/j.cep.2014.10.017
- Madalosso HB, Sousa Silva R, Merlini A, Battisti R, Machado RAF, Marangoni C. 2021. Modeling and experimental validation of direct contact membrane distillation applied to synthetic dye solutions. J Chem Technol Biotechnol. 96(4):909–922. doi:https://doi.org/10.1002/jctb.6599
- Mantelli MBH, Ângelo WB, Borges T. 2010. Performance of naphthalene thermosyphons with non-condensable gases – Theoretical study and comparison with data. Int J Heat Mass Transf. 53(17–18):3414–3428. doi:https://doi.org/10.1016/j.ijheatmasstransfer.2010.03.041
- Marangoni C, Meneguelo PA, Teleken GJ, Parisotto IGB, Werle LO, Machado RAF, Dos SM, Gomes AO, Medina LC. 2011. New configuration of a distillation process with reduced dimensions. Chem Eng Trans. 24(2000):799–804. doi:https://doi.org/10.3303/CET1124134
- Marangoni C, Machado RAF, Bolzan A. 2013. Distributed heat supply for distillation control to reduce feed composition disturbance effects. Chem Eng Technol. 36(12):2071–2079. doi:https://doi.org/10.1002/ceat.201300266
- Marangoni C, Meneguelo AP, Teleken JG, Werle LO, Milanez KW, Mantelli MBH, Quadri MB, Bolzan A, Santos Md, Medina LC, et al. 2019a. Falling film distillation column with heat transfer by means of a vapor chamber. Part I: isothermal operation. Chem Eng Commun. 206(8):994–1005. doi:https://doi.org/10.1080/00986445.2018.1542250
- Marangoni C, Peruzzo T, Parisotto IGB, Ricardo VW, Claumann CA, Milanez KW, Mantelli MBH, Quadri MB, Bolzan A, dos Santos MC, et al. 2019b. Falling film distillation column with heat transfer by means of a vapor chamber. Part II: operation with a temperature profile. Chem Eng Commun. 206(8):1006–1014. doi:https://doi.org/10.1080/00986445.2018.1542255
- Marcus Y. 1998. The properties of solvents. Vol. 4: Wiley series in solution chemistry. Chichester, UK: John Wiley & Sons.
- Mello GN, Battisti R, Urruth NS, Machado RAF, Marangoni C. 2020. New distributed-action control strategy with simultaneous heating and cooling in trays of a pilot-scale diabatic distillation column. Chem Eng Res Des. 159:424–438. doi:https://doi.org/10.1016/j.cherd.2020.05.001
- Messaâdi A, Dhouibi N, Hamda H, Belgacem FBM, Adbelkader YH, Ouerfelli N, Hamzaoui AH. 2015. A new equation relating the viscosity Arrhenius temperature and the activation energy for some Newtonian classical solvents. J Chem. 2015:1–12. doi:https://doi.org/10.1155/2015/163262
- Milanez F, Mantelli MBH. 2010. Heat transfer limit due to pressure drop of a two-phase loop thermosyphon. Heat Pipe Sci Tech. 1(3):237–250. doi:https://doi.org/10.1615/HeatPipeScieTech.2011003082
- Oliveira JLG, Tecchio C, Paiva KV, Mantelli MBH, Gandolfi R, Ribeiro LGS. 2016. In-flight testing of loop thermosyphons for aircraft cooling. Appl Therm Eng. 98:144–156. doi:https://doi.org/10.1016/j.applthermaleng.2015.12.008
- Park H, Kim Y, Jo S, Choi J, Yang S, Hee M, Kook D. 2017. Heat and mass transfer of binary distillation in a vertical wetted-wall column. Chem Eng Res Des. 128:49–58. doi:https://doi.org/10.1016/j.cherd.2017.09.032
- Parra-Santiago JJ, Guerrero-Fajardo CA, Sodré JR. 2015. Distillation process optimization for styrene production from a styrene-benzene-toluene system in a Petlyuk column. Chem Eng Process Process Intensif. 98:106–111. doi:https://doi.org/10.1016/j.cep.2015.10.017
- Portha J-F, Falk L, Commenge J-M. 2014. Local and global process intensification. Chem Eng Process Process Intensif. 84:1–13. doi:https://doi.org/10.1016/j.cep.2014.05.002
- Shenvi AA, Herron DM, Agrawal R. 2011. Energy efficiency limitations of the conventional heat integrated distillation column (HIDiC) configuration for binary distillation. Ind Eng Chem Res. 50(1):119–130. doi:https://doi.org/10.1021/ie101698f
- Spiegel L, Meier W. 2003. Distillation columns with structured packings in the next decade. Chem Eng Res Des. 81(1):39–47. doi:https://doi.org/10.1205/026387603321158177
- Teleken JG, Werle LO, Parisotto IGB, Marangoni C, Meneguelo AP, Bolzan A, Machado RAF. 2012. Computational fluid dynamics simulation of the feed distribution system of a falling film distillation device. Comput Aided Chem Eng. 31:845–849. doi:https://doi.org/10.1016/B978-0-444-59507-2.50161-X
- Van Gerven T, Stankiewicz A. 2009. Structure, energy, synergy, time—The fundamentals of process intensification. Ind Eng Chem Res. 48(5):2465–2474. doi:https://doi.org/10.1021/ie801501y
- Zierhut EJ, Battisti R, Machado RAF, Marangoni C. 2020. Distributed control strategy with Smith's predictor in a pilot‐scale diabatic distillation unit. Chem Eng Technol. 43(9):1884–1896. doi:https://doi.org/10.1002/ceat.202000102