@article{MTMT:34568149,
	title = {Exploring Exergy Performance in Tetrahydrofuran/Water and Acetone/Chloroform Separations},
	url = {https://m2.mtmt.hu/api/publication/34568149},
	author = {Jonathan, Wavomba and Mugo, G.W. and Varbanov, P.S. and Szanyi, Ágnes and Mizsey, Péter},
	doi = {10.3390/pr12010014},
	journal-iso = {PROCESSES},
	journal = {PROCESSES},
	volume = {12},
	unique-id = {34568149},
	issn = {2227-9717},
	abstract = {Distillation is significantly influenced by energy costs, prompting a need to explore effective strategies for reducing energy consumption. Among these, heat integration is a key approach, but evaluating its efficiency is paramount. Therefore, this study presents exergy as an energy quality indicator, analyzing irreversibility and efficiencies in tetrahydrofuran/water and acetone/chloroform distillations. Both systems have equimolar feed streams, yielding products with 99.99 mol% purity. The simulations are performed using Aspen Plus™, enabling evaluation at the column level, as a standalone process, or from a lean perspective that considers integration opportunities with other plants. The results show that, despite anticipated energy savings from heat integration, economic viability depends on pressure sensitivity. The results demonstrate that heat-integrated extractive distillation for acetone/chloroform raises utility energy consumption. Exergy calculations comparing standalone and total site integration reveal the variation in distillation efficiency with operation mode. Global exergy efficiency in both extractive and pressure-swing distillation depends on the fate of condenser duty. In heat-integrated extractive distillation, global exergy efficiency drops from 8.7% to 5.7% for tetrahydrofuran/water and 11.5% to 8.3% for acetone/chloroform. Similarly, heat-integrated pressure-swing distillation sees global exergy efficiency decrease from 34.2% to 23.7% for tetrahydrofuran/water and 9.5% to 3.6% for acetone/chloroform, underscoring the nuanced impact of heat integration, urging careful process design consideration. © 2023 by the authors.},
	keywords = {Computer modeling; Environmental impact; Heat integration; Process intensification; Thermodynamic efficiency; distillation energy efficiency},
	year = {2024},
	eissn = {2227-9717},
	orcid-numbers = {Mizsey, Péter/0000-0002-6976-6210}
}

@article{MTMT:34533660,
	title = {Oxyfuel Combustion Makes Carbon Capture More Efficient},
	url = {https://m2.mtmt.hu/api/publication/34533660},
	author = {Talei, Saeed and Fozer, D. and Varbanov, P.S. and Szanyi, Ágnes and Mizsey, Péter},
	doi = {10.1021/acsomega.3c05034},
	journal-iso = {ACS OMEGA},
	journal = {ACS OMEGA},
	volume = {9},
	unique-id = {34533660},
	issn = {2470-1343},
	abstract = {Fossil energy carriers cannot be totally replaced, especially if nuclear power stations are stopped and renewable energy is not available. To fulfill emission regulations, however, points such as emission sources should be addressed. Besides desulfurization, carbon capture and utilization have become increasingly important engineering activities. Oxyfuel technologies offer new options to reduce greenhouse gas emissions; however, the use of clean oxygen instead of air can be dangerous in the case of certain existing technologies. To replace the inert effect of nitrogen, carbon dioxide is mixed with oxygen gas in the case of such air combustion processes. In this work, the features of carbon capture in five different flue gases of air combustion and such oxyfuel combustion where additional carbon dioxide is mixed with clean oxygen are studied and compared. The five different flue gases originate from the gas-fired power plant, coal-fired power plant, coal-fired combined heat and power plant, the aluminum production industry, and the cement manufacturing industry. Monoethanolamine, which is an industrially preferred solvent for carbon dioxide capture from gas streams at low pressures, is selected as an absorbent, and the same amount of carbon dioxide is captured; that is, always that amount of carbon dioxide is captured, which is the result of the fossil combustion process. ASPEN Plus is used for mathematical modeling. The results show that the oxyfuel combustion cases need significantly less energy, especially at high carbon dioxide removal rates, e.g., higher than 90%, than that of the air combustion cases. The savings can even be as high as 84%. Moreover, 100% carbon capture was also be completed. This finding can be due to the fact that in the oxyfuel combustion cases, the carbon dioxide concentration is much higher than that of the air combustion cases because of the inert carbon dioxide and that higher carbon dioxide concentration results in a higher driving force for the mass transfer. The oxyfuel combustion processes also show another advantage over the air combustion processes since no nitrogen oxides are produced in the combustion process. © 2024 The Authors. Published by American Chemical Society.},
	year = {2024},
	eissn = {2470-1343},
	pages = {3250-3261},
	orcid-numbers = {Mizsey, Péter/0000-0002-6976-6210}
}

@article{MTMT:34473848,
	title = {Systematic Energy Optimization and Design of Process Alternatives for Separation of Quaternary Azeotropic Mixtures},
	url = {https://m2.mtmt.hu/api/publication/34473848},
	author = {Pimentel, Jean and Mizsey, Péter},
	doi = {10.3303/CET23107096},
	journal-iso = {CHEM ENG TR},
	journal = {CHEMICAL ENGINEERING TRANSACTIONS},
	volume = {107},
	unique-id = {34473848},
	issn = {1974-9791},
	year = {2023},
	eissn = {2283-9216},
	pages = {571-576},
	orcid-numbers = {Pimentel, Jean/0000-0003-3359-4848; Mizsey, Péter/0000-0002-6976-6210}
}

@article{MTMT:34406416,
	title = {Analysis of Molecular Dynamics Simulation of Carbonic Anhydrase},
	url = {https://m2.mtmt.hu/api/publication/34406416},
	author = {Talei, Saeed and Hadjadj, Rachid and Mizsey, Péter and Owen, Michael Christopher},
	doi = {10.32974/mse.2022.011},
	journal-iso = {HUNG MATER CHEM SCI ENG},
	journal = {HUNGARIAN MATERIALS AND CHEMICAL SCIENCES AND ENGINEERING},
	volume = {47},
	unique-id = {34406416},
	issn = {3004-0000},
	year = {2023},
	eissn = {3004-0817},
	pages = {109-117},
	orcid-numbers = {Mizsey, Péter/0000-0002-6976-6210}
}

@article{MTMT:34096187,
	title = {Hybrid prediction-driven high-throughput sustainability screening for advancing waste-to-dimethyl ether valorization},
	url = {https://m2.mtmt.hu/api/publication/34096187},
	author = {Fózer, Dániel and Philippe, Nimmegeers and Tóth, András József and Petar, Sabev Varbanov and Jiří, Jaromír Klemeš and Mizsey, Péter and Michael, Zwicky Hauschild and Mikołaj, Owsianiak},
	doi = {10.1021/acs.est.3c01892},
	journal-iso = {ENVIRON SCI TECHNOL},
	journal = {ENVIRONMENTAL SCIENCE & TECHNOLOGY},
	volume = {57},
	unique-id = {34096187},
	issn = {0013-936X},
	year = {2023},
	eissn = {1520-5851},
	pages = {13449-13462},
	orcid-numbers = {Tóth, András József/0000-0002-5787-8557; Mizsey, Péter/0000-0002-6976-6210}
}

@article{MTMT:33854809,
	title = {CFD Investigation of Dry Tray Pressure Drop of Perforated Trays without Downcomer},
	url = {https://m2.mtmt.hu/api/publication/33854809},
	author = {Kállai, Viktória and Mizsey, Péter and Szepesi L., Gábor},
	doi = {10.3311/PPch.21914},
	journal-iso = {PERIOD POLYTECH CHEM ENG},
	journal = {PERIODICA POLYTECHNICA-CHEMICAL ENGINEERING},
	volume = {67},
	unique-id = {33854809},
	issn = {0324-5853},
	abstract = {The dry tray pressure drop behaviors in trays without downcomer with different inclination of holes (standard, 75°, 60° and 45°) and tray thickness (2.5, 5, and 10 mm) are investigated. The trays are investigated using computational fluid dynamics (CFD) in Ansys Fluent® software. 20 °C air was used to represent the gas phase with 20–50 m3/h flow rates. The column there are four trays with 7 mm of hole diameter.The CFD results determined that the higher angle of the holes with respect to the tray causes smaller dry tray pressure drop and turbulence intensity in the gas flow. Furthermore, in 75° hole inclined perforated tray and the standard hole the dry tray pressure drop is similar. From the simulation results it is also determined that in case of higher tray thickness the dry tray pressure drop is lower.On the basis of the CFD simulation results some correlations can be determined for the calculation of the dry tray pressure drop of the different trays.},
	year = {2023},
	eissn = {1587-3765},
	pages = {310-315},
	orcid-numbers = {Kállai, Viktória/0000-0002-7710-5762; Mizsey, Péter/0000-0002-6976-6210; Szepesi L., Gábor/0000-0003-0942-374X}
}

@article{MTMT:33784071,
	title = {Dynamic Controllability Study of Extractive and Pressure‐Swing Distillations for Tetrahydrofuran/Water Separation},
	url = {https://m2.mtmt.hu/api/publication/33784071},
	author = {Mtogo, Jonathan Wavomba and Mugo, Gladys Wanyaga and Mizsey, Péter},
	doi = {10.1002/ceat.202300006},
	journal-iso = {CHEM ENG TECHNOL},
	journal = {CHEMICAL ENGINEERING & TECHNOLOGY},
	volume = {46},
	unique-id = {33784071},
	issn = {0930-7516},
	year = {2023},
	eissn = {1521-4125},
	pages = {1706-1716},
	orcid-numbers = {Mizsey, Péter/0000-0002-6976-6210}
}

@article{MTMT:33458701,
	title = {Effects of Energy Intensification of Pressure-Swing Distillation on Energy Consumption and Controllability},
	url = {https://m2.mtmt.hu/api/publication/33458701},
	author = {Jonathan, Wavomba and Tóth, András József and Fózer, Dániel and Mizsey, Péter and Szanyi, Ágnes},
	doi = {10.1021/acsomega.2c05959},
	journal-iso = {ACS OMEGA},
	journal = {ACS OMEGA},
	volume = {8},
	unique-id = {33458701},
	issn = {2470-1343},
	year = {2023},
	eissn = {2470-1343},
	pages = {726-736},
	orcid-numbers = {Tóth, András József/0000-0002-5787-8557; Mizsey, Péter/0000-0002-6976-6210}
}

@article{MTMT:32860717,
	title = {Physicochemical methods for process wastewater treatment: powerful tools for circular economy in the chemical industry},
	url = {https://m2.mtmt.hu/api/publication/32860717},
	author = {Tóth, András József and Fózer, Dániel and Mizsey, Péter and Varbanov, Petar and Klemeš, Jiri Jaromir},
	doi = {10.1515/revce-2021-0094},
	journal-iso = {REVCE},
	journal = {REVIEWS IN CHEMICAL ENGINEERING},
	volume = {39},
	unique-id = {32860717},
	issn = {0167-8299},
	year = {2023},
	eissn = {2191-0235},
	pages = {1123-1151},
	orcid-numbers = {Tóth, András József/0000-0002-5787-8557; Mizsey, Péter/0000-0002-6976-6210}
}

@article{MTMT:33541104,
	title = {Comparison of Carbon Capture process for Coal-fired and Gas-fired Power Plants},
	url = {https://m2.mtmt.hu/api/publication/33541104},
	author = {Talei, Saeed and Mizsey, Péter},
	journal-iso = {Doktorandusz Almanach},
	journal = {Doktorandusz Almanach},
	volume = {1},
	unique-id = {33541104},
	issn = {2939-7294},
	year = {2022},
	pages = {158-165},
	orcid-numbers = {Mizsey, Péter/0000-0002-6976-6210}
}