Related Experiment Video
Updated: Jan 17, 2026

Preparation of Binary and Ternary Deep Eutectic Systems
Published on: October 31, 2019
Finding Sustainable Deep Eutectic Solvents for an Efficient Separation of CO2 and NH3 in Melamine Production with
Luan Vittor Tavares Duarte de Alencar1,2, Sabrina Belén Rodríguez-Reartes1,3,4, Frederico Wanderley Tavares2,5
1Department of Chemical Engineering, ETSEQ, Universitat Rovira i Virgili, Avinguda Països Catalans 26, 43007 Tarragona, Spain.
Abstract:
Industrial processes frequently release tail gases containing harmful components, such as carbon dioxide (CO2) and ammonia (NH3), with significant environmental implications. Effective separation and recovery of these gases are critical for reducing pollution and enhancing resource efficiency. This paper investigates the use of deep eutectic solvents (DESs) to capture and separate CO2 and NH3 from melamine production tail gases, offering an alternative to traditional methods such as coproduction systems and water scrubbing. Choline chloride ([Ch]-Cl)-based solvents with ethylene glycol (EG), urea (UR), and glycerol (GL) are assessed for selective gas absorption using the soft-SAFT Equation of State (EoS). This approach has been used to model the solubility of CO2 and NH3 in these DESs and evaluate key properties, including absorption isotherms, enthalpy, entropy of dissolution, effective Henry's constants, and ideal selectivity. Results reveal that the presence of EG enhances the NH3 absorption capacity, while UR shows higher CO2 absorption. From this information, the competitive selectivity in a standard melamine tail gas mixture (60% NH3 and 40% CO2 in mole fraction) and DESs has been predicted. Among them, [Ch]-Cl:EG shows the best selectivity, and the 1:7 proportion provides the optimal value for NH3/CO2 separation. This work highlights the potential of DESs for efficient gas separation, emphasizing the utility of molecular modeling as a precursor to experimental validation in the design of sustainable separation processes.

