@article{MTMT:32774148,
	title = {Low-Cost and Efficient Solution for the Automation of Laboratory Scale Experiments: The Case of Distillation Column},
	url = {https://m2.mtmt.hu/api/publication/32774148},
	author = {Enyedi, Flórián and Do Thi, Huyen Trang and Szanyi, Ágnes and Mizsey, Péter and Tóth, András József and Nagy, Tibor},
	doi = {10.3390/pr10040737},
	journal-iso = {PROCESSES},
	journal = {PROCESSES},
	volume = {10},
	unique-id = {32774148},
	issn = {2227-9717},
	year = {2022},
	eissn = {2227-9717},
	orcid-numbers = {Mizsey, Péter/0000-0002-6976-6210; Tóth, András József/0000-0002-5787-8557}
}

@article{MTMT:31957202,
	title = {Modelling of Organophilic and Hydrophilic Pervaporations for Separation of Ethyl Acetate – water Mixture},
	url = {https://m2.mtmt.hu/api/publication/31957202},
	author = {Tóth, András József and Haáz, Enikő and Ladanyi, R. and Szilágyi, Botond and Fózer, Dániel and Selim, Asmaa Khaled Mohamed and Nagy, Tibor and Mizsey, Péter},
	doi = {10.1016/B978-0-12-823377-1.50127-0},
	journal-iso = {COMPAIDED CHEMI ENG},
	journal = {COMPUTER-AIDED CHEMICAL ENGINEERING},
	volume = {48},
	unique-id = {31957202},
	issn = {1570-7946},
	abstract = {Pervaporation is a separation method that is considered as green technology because of its low energy consumption. The mechanism of component separation in a liquid mixture by pervaporation is complex but it can be explained with the solution-diffusion mechanism. The work is motivated by an industrial separation problem, that is, ethyl acetate removal from aqueous mixture. To complete this goal hybrid organophilic/hydrophilic pervaporation of ethyl acetate/water mixture through commercially available Sulzer PERVAP™ 4060 and 1510 membranes are investigated to obtain information about the removal of ethyl acetate. Our experimental data are evaluated with the pervaporation model of our improvement (Valentínyi et al., 2013) and it is found that the model can be applied also for both cases. The hybrid separation process is rigorously modelled in professional flowsheet environment, and optimized with the dynamic programming optimization method. The objective function is product purity of 99.0, 99.5 m/m% in water and ethyl acetate content and the total annual cost is also determined. It can be determined, this hybrid separation should be become the alternative of distillation if the energy prices are too high. © 2020 Elsevier B.V.},
	keywords = {ethyl acetate removal; flowsheet environment; model optimization; organophilic and hydrophilic pervaporation},
	year = {2020},
	pages = {757-762},
	orcid-numbers = {Tóth, András József/0000-0002-5787-8557; Haáz, Enikő/0000-0002-7032-1040; Szilágyi, Botond/0000-0001-7777-9612; Mizsey, Péter/0000-0002-6976-6210}
}

@article{MTMT:30803970,
	title = {Laponite /PVA Pervaporation membrane for desalinating simulated RO high-salinity by-product},
	url = {https://m2.mtmt.hu/api/publication/30803970},
	author = {Selim, Asmaa Khaled Mohamed and Tóth, András József and Fózer, Dániel and Haáz, Enikő and Nagy, Tibor and Mizsey, Péter},
	doi = {10.5004/dwt.2020.24912},
	journal-iso = {DESALIN WATER TREAT},
	journal = {DESALINATION AND WATER TREATMENT},
	volume = {175},
	unique-id = {30803970},
	issn = {1944-3994},
	year = {2020},
	eissn = {1944-3986},
	pages = {24-31},
	orcid-numbers = {Tóth, András József/0000-0002-5787-8557; Haáz, Enikő/0000-0002-7032-1040; Mizsey, Péter/0000-0002-6976-6210}
}

@article{MTMT:30374776,
	title = {Experimental investigation and modeling of the separation of ternary mixtures by hydrophilic pervaporation},
	url = {https://m2.mtmt.hu/api/publication/30374776},
	author = {Valentínyi, Nóra and André, Anita and Haáz, Enikő and Fózer, Dániel and Tóth, András József and Nagy, Tibor and Mizsey, Péter},
	doi = {10.1080/01496395.2019.1569692},
	journal-iso = {SEP SCI TECHNOL},
	journal = {SEPARATION SCIENCE AND TECHNOLOGY},
	volume = {55},
	unique-id = {30374776},
	issn = {0149-6395},
	year = {2020},
	eissn = {1520-5754},
	pages = {601-617},
	orcid-numbers = {Haáz, Enikő/0000-0002-7032-1040; Tóth, András József/0000-0002-5787-8557; Mizsey, Péter/0000-0002-6976-6210}
}

@inproceedings{MTMT:31951819,
	title = {Modelling of extractive heterogeneous-azeotropic distillation in dividing wall column},
	url = {https://m2.mtmt.hu/api/publication/31951819},
	author = {Tóth, András József and Fózer, Dániel and Nagy, Tibor and Haáz, Enikő and Nagy, Judit and Mizsey, Péter},
	booktitle = {29TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING, PT A},
	doi = {10.1016/B978-0-12-818634-3.50040-0},
	unique-id = {31951819},
	abstract = {The distillation based separation can be extremely complex if highly non-ideal mixtures are to be separated. In spite of different successfully applied unit operations there is always a possible way to improve the distillation technique and widen its toolbar. A novel improvement in this area is the development of the extractive heterogeneous-azeotropic distillation (EHAD). For the sake of the demonstration of the efficient use of EHAD in Dividing wall columns (DWC), two quaternary mixtures are selected for separation: Water – Ethanol – Ethyl acetate – Acetone and Water – Ethanol – Ethyl acetate – Ethylene glycol. There are real waste mixtures from pharmaceutical industry. It must be mentioned, extractive heterogeneous-azeotropic distillation method has never been investigated in dividing wall columns. Conventional distillation column sequences and dividing wall columns are selected for comparison. Rigorous steady-state simulations are carried out using ChemCAD flowsheet simulation software. Number of trays, heat duties and Total Annual Cost (TAC) of the systems are optimized. It can be concluded, the application of the EHAD in DWCs allows also the simplification of the separation schemes and the separation reduces the energy requirements of the distillation and opens new horizons for the separation of non-ideal mixtures saving energy, money and natural resources. Using DWCs the reboiler duties can be reduced with 20% and the appropriate separation can be reached with one less column. © 2019 Elsevier B.V.},
	keywords = {extractive heterogeneous-azeotropic distillation; Non-ideal mixtures; Dividing wall column; flowsheet simulator},
	year = {2019},
	pages = {235-240},
	orcid-numbers = {Tóth, András József/0000-0002-5787-8557; Haáz, Enikő/0000-0002-7032-1040; Mizsey, Péter/0000-0002-6976-6210}
}

@article{MTMT:30884106,
	title = {Megújuló energia tárolásának és értéknövelt termék előállításának vizsgálata mikroalga biomassza felhasználásával},
	url = {https://m2.mtmt.hu/api/publication/30884106},
	author = {Fózer, Dániel and Nagy, Tibor and Tóth, András József and Mizsey, Péter},
	journal-iso = {CIRC ECON ENVIRON PROTECT},
	journal = {KÖRFORGÁSOS GAZDASÁG ÉS KÖRNYEZETVÉDELEM / CIRCULAR ECONOMY AND ENVIRONMENTAL PROTECTION},
	volume = {3},
	unique-id = {30884106},
	year = {2019},
	eissn = {2560-1024},
	pages = {5-14},
	orcid-numbers = {Tóth, András József/0000-0002-5787-8557; Mizsey, Péter/0000-0002-6976-6210}
}

@{MTMT:30782148,
	title = {Sustainable, hybrid method for VOC removal from pharmaceutical process wastewater: distillation and hydrophilic pervaporation},
	url = {https://m2.mtmt.hu/api/publication/30782148},
	author = {Tóth, András József and Haáz, Enikő and Nagy, Tibor and Fózer, Dániel and André, Anita and Selim, Asmaa Khaled Mohamed and Mizsey, Péter},
	booktitle = {PERMEA 2019 - Membrane Conference of Visegrád Countries - Program and Book of Abstracts},
	unique-id = {30782148},
	year = {2019},
	pages = {53},
	orcid-numbers = {Tóth, András József/0000-0002-5787-8557; Haáz, Enikő/0000-0002-7032-1040; Mizsey, Péter/0000-0002-6976-6210}
}

@article{MTMT:30711851,
	title = {Flexible and efficient solution for control problems of chemical laboratories},
	url = {https://m2.mtmt.hu/api/publication/30711851},
	author = {Nagy, Tibor and Enyedi, Flórián and Haáz, Enikő and Fózer, Dániel and Tóth, András József and Mizsey, Péter},
	doi = {10.1016/B978-0-12-818634-3.50304-0},
	journal-iso = {COMPAIDED CHEMI ENG},
	journal = {COMPUTER-AIDED CHEMICAL ENGINEERING},
	volume = {46},
	unique-id = {30711851},
	issn = {1570-7946},
	year = {2019},
	pages = {1819-1824},
	orcid-numbers = {Haáz, Enikő/0000-0002-7032-1040; Tóth, András József/0000-0002-5787-8557; Mizsey, Péter/0000-0002-6976-6210}
}

@article{MTMT:30655027,
	title = {Enhanced separation of maximum boiling azeotropic mixtures with extractive heterogeneous-azeotropic distillation},
	url = {https://m2.mtmt.hu/api/publication/30655027},
	author = {Tóth, András József and Szilágyi, Botond and Haáz, Enikő and Solti, Szabolcs and Nagy, Tibor and Szanyi, Ágnes and Nagy, Judit and Mizsey, Péter},
	doi = {10.1016/j.cherd.2019.05.002},
	journal-iso = {CHEM ENG RES DES},
	journal = {CHEMICAL ENGINEERING RESEARCH AND DESIGN},
	volume = {147},
	unique-id = {30655027},
	issn = {0263-8762},
	year = {2019},
	eissn = {1744-3563},
	pages = {55-62},
	orcid-numbers = {Tóth, András József/0000-0002-5787-8557; Haáz, Enikő/0000-0002-7032-1040; Mizsey, Péter/0000-0002-6976-6210}
}

@{MTMT:30650268,
	title = {Alkohol-víz elegyek elválasztási eljárásainak összehasonlítása: desztilláció és pervaporáció},
	url = {https://m2.mtmt.hu/api/publication/30650268},
	author = {Tóth, András József and Haáz, Enikő and Fózer, Dániel and André, Anita and Nagy, Tibor},
	booktitle = {Műszaki Kémiai Napok 2019: Chemical Engineering Conference 2019},
	unique-id = {30650268},
	year = {2019},
	pages = {95},
	orcid-numbers = {Tóth, András József/0000-0002-5787-8557; Haáz, Enikő/0000-0002-7032-1040}
}