Process simulation coupled with LCA for the evaluation of liquid - liquid extraction processes of phenol from aqueous streams

2021 ◽  
Vol 41 ◽  
pp. 102077
Author(s):  
Letitia Petrescu ◽  
Silvia Burca ◽  
Maurizio Fermeglia ◽  
Andrea Mio ◽  
Calin-Cristian Cormos
Processes ◽  
2020 ◽  
Vol 8 (10) ◽  
pp. 1220
Author(s):  
Diego Rodríguez-Llorente ◽  
Andrés Cañada-Barcala ◽  
Silvia Álvarez-Torrellas ◽  
Vicente Ismael Águeda ◽  
Juan García ◽  
...  

Diverse and abundant applications of the eutectic solvents have appeared in the last years. Their promising tunable properties, eco-friendly character and the possibility of being prepared from numerous compounds have led to the publication of numerous papers addressing their use in different areas. Terpenes and terpenoids have been employed in the formulation of eutectic solvents, though they also have been applied as solvents in extraction processes. For their hydrophobic nature, renewable character, low environmental impact, cost and being non-hazardous, they have also been proposed as possible substitutes of conventional solvents in the separation of organic compounds from aqueous streams, similarly to hydrophobic eutectic solvents. The present work reviews the application of eutectic solvents in liquid–liquid extraction and terpenes and terpenoids in extraction processes. It has been made a research in the current state-of-the-art in these fields, describing the proposed applications of the solvents. It has been highlighted the scale-up feasibility, solvent regeneration and reuse procedures and the comparison of the performance of eutectic solvents, terpenes and terpenoids in extraction with conventional organic solvents or ionic liquids. Ultimately, it has been also discussed the employ of predictive methods in extraction, the reliability of thermodynamic models in correlation of liquid–liquid equilibria and simulation of liquid–liquid extraction processes.


2021 ◽  
Author(s):  
Fabian Jirasek ◽  
Jakob Burger ◽  
Hans Hasse

The conceptual design of fluid separation processes is particularly challenging if the considered mixtures are poorly specified, since classical thermodynamic models cannot be applied when the composition is unknown. We have recently developed a method (NEAT) to predict activity coefficients in such mixtures. It combines the thermodynamic group contribution concept with the ability of NMR spectroscopy to quantify chemical groups. In the present work, we describe how NEAT can be applied to equilibrium stage simulations of liquid–liquid extraction processes with poorly specified feeds. Only a single 13C NMR spectrum of the feed is needed for predicting the distribution of a target component for different process parameters, such as temperature or extracting agent. The predictions from several test cases are compared to results that are obtained using the full knowledge on the composition of the feed and surprisingly good agreement is found.


1996 ◽  
pp. 551-576 ◽  
Author(s):  
M. G. Carneiro-Da-Cunha ◽  
E. P. Melo ◽  
M. J. Sebastião ◽  
M. R. Aires-Barros ◽  
J. M. S. Cabral

2014 ◽  
Vol 16 (16) ◽  
pp. 7339 ◽  
Author(s):  
Christophe Déjugnat ◽  
Sandrine Dourdain ◽  
Véronique Dubois ◽  
Laurence Berthon ◽  
Stéphane Pellet-Rostaing ◽  
...  

2018 ◽  
Vol 47 (32) ◽  
pp. 10906-10914 ◽  
Author(s):  
Patrik Weßling ◽  
Michael Trumm ◽  
Andreas Geist ◽  
Petra J. Panak

N,N′-Dimethyl,N,N′-dioctylhexylethoxymalonamide (DMDOHEMA) is used to separate An(iii) and Ln(iii) from fission products in several liquid–liquid extraction processes that aim at recycling actinides.


2018 ◽  
Vol 137 ◽  
pp. 510-533 ◽  
Author(s):  
Ehsan Reyhanitash ◽  
Thomas Brouwer ◽  
Sascha R.A. Kersten ◽  
A.G.J. van der Ham ◽  
Boelo Schuur

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