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https://doi.org/10.2139/ssrn.4672543
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Outgoing claims: the papers this work cites, builds on, or argues with.
inferredcites →https://doi.org/10.1002/9781118938607.ch7openalex-extracted
Vapour‐Liquid Equilibrium, Viscosity and Interfacial Tension Modelling of Aqueous Solutions of Ethylene Glycol or Triethylene Glycol in the Presence of Methane, Carbon Dioxide and Hydrogen Sulfide
inferredcites →https://doi.org/10.1016/0009-2509(72)80096-4openalex-extracted
Equilibrium constants from a modified Redlich-Kwong equation of state
inferredcites →https://doi.org/10.1016/0140-6701(96)91019-xopenalex-extracted
96/01121 BP statistical review of world energy 1995
inferredcites →https://doi.org/10.1016/0378-3812(87)85018-5openalex-extracted
Vapor liquid equilibria for acid gases and lower alkanes in triethylene glycol
inferredcites →https://doi.org/10.1016/b978-0-7506-7776-9.x5000-3openalex-extracted
Handbook of Natural Gas Transmission and Processing
inferredcites →https://doi.org/10.1016/b978-1-85617-980-5.00001-xopenalex-extracted
Hydrate Prediction and Prevention
inferredcites →https://doi.org/10.1016/j.cjche.2020.03.013openalex-extracted
A computational simulation study for techno-economic comparison of conventional and stripping gas methods for natural gas dehydration
inferredcites →https://doi.org/10.1016/j.fluid.2007.11.017openalex-extracted
Measurement of the triethylene glycol solubility in supercritical methane at pressures up to 9MPa
inferredcites →https://doi.org/10.1016/j.fluid.2011.08.009openalex-extracted
P–x data for binary systems using a novel static total pressure apparatus
inferredcites →https://doi.org/10.1016/j.fluid.2011.12.025openalex-extracted
Experimental study and phase equilibrium modeling of systems containing acid gas and glycol
inferredcites →https://doi.org/10.1016/j.fluid.2016.03.007openalex-extracted
Carbon dioxide solubility in Triethylene Glycol and aqueous solutions
inferredcites →https://doi.org/10.1016/j.fluid.2018.08.017openalex-extracted
Experimental measurement of carbon dioxide solubility in 1-methylpyrrolidin-2-one (NMP) + 1-butyl-3-methyl-1H-imidazol-3-ium tetrafluoroborate ([bmim][BF4]) mixtures using a new static-synthetic cell
inferredcites →https://doi.org/10.1016/j.fluid.2022.113475openalex-extracted
Experimental measurements of CO2 solubility, viscosity, density, sound velocity and evaporation rate for 2-(2-aminoethoxy)ethanol (DGA) + 1-methylpyrrolidin-2-one (NMP) / water + ionic liquid systems
inferredcites →https://doi.org/10.1016/j.jct.2008.12.022openalex-extracted
Vapour pressures, densities, and viscosities of the aqueous solutions containing (triethylene glycol or propylene glycol) and (LiCl or LiBr)
inferredcites →https://doi.org/10.1016/j.jct.2015.07.003openalex-extracted
Modelling phase equilibria for acid gas mixtures using the CPA equation of state. Part VI. Multicomponent mixtures with glycols relevant to oil and gas and to liquid or supercritical CO2 transport applications
inferredcites →https://doi.org/10.1016/j.jngse.2018.06.008openalex-extracted
Revamping existing glycol technologies in natural gas dehydration to improve the purity and absorption efficiency: Available methods and recent developments
inferredcites →https://doi.org/10.1016/j.molliq.2012.09.015openalex-extracted
Volumetric, viscosimetric and surface properties of aqueous solutions of triethylene glycol, tetraethylene glycol, and tetraethylene glycol dimethyl ether
inferredcites →https://doi.org/10.1016/j.molliq.2013.07.016openalex-extracted
Solubility and density of carbon dioxide in different aqueous alkanolamine solutions blended with 1-butyl-3-methylimidazolium acetate ionic liquid at high pressure
inferredcites →https://doi.org/10.1016/j.supflu.2013.11.021openalex-extracted
Synthetic methods in phase equilibria: A new apparatus and error analysis of the method
inferredcites →https://doi.org/10.1021/acs.jced.0c00198openalex-extracted
Experimental Measurement and Thermodynamic Modeling of Methane Solubility in Triethylene Glycol within the Temperature Range of 343.16–444.95 K
inferredcites →https://doi.org/10.1021/acs.jced.0c00618openalex-extracted
Investigation of Mixed MEA-Based Solvents Featuring Ionic Liquids and NMP for CO2 Capture: Experimental Measurement of CO2 Solubility and Thermophysical Properties
inferredcites →https://doi.org/10.1021/acs.jced.1c00313openalex-extracted
Phase Behavior in Natural Gas + Glycol Systems, Part 1: Tri(ethylene glycol) (TEG) and Its Aqueous Solutions
inferredcites →https://doi.org/10.1021/acs.jced.2c00597openalex-extracted
Vapor–Liquid Equilibrium Measurements and Cubic-Plus-Association Modeling of Triethylene Glycol + Water + Methane Systems at 6.0 and 12.5 MPa
inferredcites →https://doi.org/10.1021/acs.jced.3c00028openalex-extracted
Investigation of the Solubility of Methane and Ethane in Hybrid Sweetening Solutions of 2-Aminoethanol and 1-Methylpyrrolidin-2-one/Water
inferredcites →https://doi.org/10.1021/i160057a011openalex-extracted
A New Two-Constant Equation of State
inferredcites →https://doi.org/10.1021/ie048832jopenalex-extracted
Application of the Cubic-Plus-Association (CPA) Equation of State to Cross-Associating Systems
inferredcites →https://doi.org/10.1021/ie801412yopenalex-extracted
Thermodynamics of Triethylene Glycol and Tetraethylene Glycol Containing Systems Described by the Cubic-Plus-Association Equation of State
inferredcites →https://doi.org/10.1021/ie9600203openalex-extracted
An Equation of State for Associating Fluids
inferredcites →https://doi.org/10.1021/je0498560openalex-extracted
High-Pressure Vapor−Liquid Equilbria of Some Carbon Dioxide + Organic Binary Systems
inferredcites →https://doi.org/10.1021/je800675uopenalex-extracted
Vapor−Liquid Equilibria of Water + Triethylene Glycol (TEG) and Water + TEG + Toluene at 85 kPa
inferredcites →https://doi.org/10.1080/00401706.1973.10489037openalex-extracted
The Estimation of Parameters in Nonlinear, Implicit Models
inferredcites →https://doi.org/10.2118/10284-msopenalex-extracted
Rigorous Computer Simulation of CO2 Dehydration Facilities
inferredcites →https://doi.org/10.2523/110009-msopenalex-extracted
Application of the CPA Equation of State to Reservoir Fluids in Presence of Water and Polar Chemicals
inferredcites →https://doi.org/10.6028/nist.tn.1297openalex-extracted
Guidelines for evaluating and expressing the uncertainty of NIST measurement results
inferredcites →https://doi.org/10.70675/985b0a1cz9263z42d5z9ef6z0659e774d789openalex-extracted
Hydrate Mitigation in Sour and Acid Gases
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