(55a) Process Design of Light Naphtha Purification By Type III Deep Eutectic Solvents
AIChE Annual Meeting
2020
2020 Virtual AIChE Annual Meeting
Fuels and Petrochemicals Division
Conceptual Process Design and Operational Improvements in Refining, Petrochemicals and Gas Processing
Monday, November 16, 2020 - 8:00am to 8:15am
Proposed Solution: In this study, conductor like screening model (COSMO) was adopted to screen suitable HBA (quaternary ammonium and polyphenol phosphonium salts) and HBD (glycol, glycerol, and carboxylic acids) for the removal of BTX from light naphtha (modeled as pentane) based on selectivity and maximum capacity. The best performing DES where then evaluated in a technoeconomic analysis model and compared to sulfolane. A model process consisting of an absorber, desorption unit, solvent regeneration and heat recovery system was used with each of the selected DESâs thermophysical properties to obtain mass and energy balances for a naphtha purification process. Processing parameters such as maximum temperature and pressure were kept similar to sulfolane, with temperatures below 100°C and pressures 2 atm. This process was designed partially in ASPEN. A sensitivity analysis evaluating the effect of key parameters such as capacity, selectivity, heat recovery, etc., was used to determine which variables should be prioritized in guiding future endeavors to modify physical absorption units for use with DES.