Hydrocarbon Extraction with Ionic Liquids
Separation and reaction processes are key components employed in the modern chemical
industry, and the former accounts for the majority of the energy consumption therein. In …
industry, and the former accounts for the majority of the energy consumption therein. In …
Generalized electrolyte‐NRTL model for mixed‐solvent electrolyte systems
A generalized electrolyte Non‐Random Two‐Liquid (eNRTL) model proposed by Chen and
coworkers is presented as a comprehensive excess Gibbs energy expression to represent …
coworkers is presented as a comprehensive excess Gibbs energy expression to represent …
Symmetric electrolyte nonrandom two-liquid activity coefficient model
The electrolyte nonrandom two-liquid (eNRTL) model is reformulated as a symmetric activity
coefficient model with the reference states chosen to be pure liquids for solvents and pure …
coefficient model with the reference states chosen to be pure liquids for solvents and pure …
Thermodynamics of fluid‐phase equilibria for standard chemical engineering operations
JM Prausnitz, FW Tavares - AIChE journal, 2004 - Wiley Online Library
Thermodynamics provides one of the scientific cornerstones of chemical engineering. This
review considers how thermodynamics is and has been used to provide phase equilibria as …
review considers how thermodynamics is and has been used to provide phase equilibria as …
[PDF][PDF] Applied thermodynamics for process modeling
CC Chen, PM Mathias - AIChE Journal, 2002 - katibeha.com
The process industries spend an estimated $500 billion annual-ly worldwide in conceptual
design, process engineering, detailed engineering, construction, startup, plant operations …
design, process engineering, detailed engineering, construction, startup, plant operations …
Thermodynamics of solvent-driven water extraction from hypersaline brines using dimethyl ether
Solvent-driven water extraction (SDWE) has promising applications in hypersaline brine
desalination, including zero-liquid discharge processing for industrial wastewaters, and …
desalination, including zero-liquid discharge processing for industrial wastewaters, and …
Modeling of mixed-solvent electrolyte systems
S Ahmed, N Ferrando, JC De Hemptinne… - Fluid Phase …, 2018 - Elsevier
Abstract Models for mixed-solvent strong electrolytes, using an equation of state (EoS) are
reviewed in this work. Through the example of ePPC-SAFT (that includes a Born term and …
reviewed in this work. Through the example of ePPC-SAFT (that includes a Born term and …
The refined e-NRTL model applied to CO2–H2O–alkanolamine systems
ET Hessen, T Haug-Warberg, HF Svendsen - Chemical Engineering …, 2010 - Elsevier
The electrolyte NRTL (e-NRTL) model by Chen (1982) and Chen and Evans (1986) is
perhaps the most commonly used activity coefficient based thermodynamic model for …
perhaps the most commonly used activity coefficient based thermodynamic model for …
Refined electrolyte‐NRTL model: Activity coefficient expressions for application to multi‐electrolyte systems
The influence of simplifying assumptions of the electrolyte‐nonrandom two‐liquid (NRTL)
model in the derivation of activity coefficient expressions as applied to multi‐electrolyte …
model in the derivation of activity coefficient expressions as applied to multi‐electrolyte …
Impact of extended long-range electrostatics on the correlation of liquid-liquid equilibria in aqueous ionic liquid systems
H Marques, AG de Castilla, S Müller, I Smirnova - Fluid phase equilibria, 2023 - Elsevier
Recently an improved long-range model for electrolyte solutions was developed that is
applicable from infinite dilution to pure salt. This paper tests this claim for the first time …
applicable from infinite dilution to pure salt. This paper tests this claim for the first time …