Zobrazeno 1 - 5
of 5
pro vyhledávání: '"Jesús David Quintero-Arias"'
Publikováno v:
Catalysts, Vol 13, Iss 2, p 284 (2023)
This study reports the analysis and design of a liquid phase esterification process to convert acetic acid with isoamyl alcohol into isoamyl acetate via reactive pervaporation, in the presence of an Amberlite IR-120 ion exchange resin catalyst. To ac
Externí odkaz:
https://doaj.org/article/3acd039cc23f4696a8c9b3ee391afb36
Publikováno v:
Case Studies in Chemical and Environmental Engineering, Vol 9, Iss , Pp 100720- (2024)
A two-stage sequential treatment of lime-assisted alum Coagulation-Flocculation (CF) and Fenton-Neutralization (F–N) was applied to industrial textile wastewater (ITWW) highly contaminated with Acid Black 194 dye. Lime-assisted alum CF at optimal o
Externí odkaz:
https://doaj.org/article/62eb12611a204800948692ad2eeb0329
Publikováno v:
Case Studies in Chemical and Environmental Engineering, Vol 9, Iss , Pp 100672- (2024)
This study successfully applied Fenton-Neutralization process (F–N) for the treatment of industrial textile wastewater polluted with highly concentrated acid black 194 dye. At optimal operating conditions (F: [Fe2+]0 = 834 mg/L, [H2O2]0 = 6078 mg/L
Externí odkaz:
https://doaj.org/article/f02c42e0bf89414aa6903bd7ad5e0bf4
Autor:
Izabela Dobrosz-Gómez, Miguel Duque-Bernal, Javier Fontalvo, Wilmar Osorio-Viana, Jesús David Quintero-Arias, Miguel Ángel Gómez-García
Publikováno v:
Fluid Phase Equilibria. 345:68-80
A new set of parameters for NRTL activity coefficient model was correlated, for the quaternary mixture acetic acid/isoamyl alcohol/isoamyl acetate/water based on the experimental vapor–liquid and liquid–liquid equilibrium data. A complete and con
Autor:
Jesús-David Quintero-Arias, Miguel Ángel Gómez-García, Wilmar Osorio-Viana, Izabela Dobrosz-Gómez, Javier Fontalvo
Publikováno v:
Desalination and Water Treatment. 51:2377-2386
Fuel ethanol production by fermentation generates isoamyl alcohol as by-product. Its conversion to isoamyl acetate is an alternative to obtain a higher value product. An intensified reaction–pervaporation process is an attractive option compared to