Review of thermodynamic properties of refrigerants+ lubricant oils KN Marsh, ME Kandil Fluid Phase Equilibria 199 (1-2), 319-334, 2002 | 156 | 2002 |
Measurement of the viscosity, density, and electrical conductivity of 1-hexyl-3-methylimidazolium bis (trifluorosulfonyl) imide at temperatures between (288 and 433) K and … ME Kandil, KN Marsh, ARH Goodwin Journal of Chemical & Engineering Data 52 (6), 2382-2387, 2007 | 135 | 2007 |
Vibrating Wire Viscometer with Wire Diameters of (0.05 and 0.15) mm: Results for Methylbenzene and Two Fluids with Nominal Viscosities at T= 298 K and p= 0.01 MPa of (14 and … ME Kandil, KN Marsh, ARH Goodwin Journal of Chemical & Engineering Data 50 (2), 647-655, 2005 | 46 | 2005 |
Measurements of electrical resistivity, NMR pore size and distribution, and x-ray CT-scan for performance evaluation of CO2 injection in carbonate rocks: A pilot study AR Adebayo, ME Kandil, TM Okasha, ML Sanni International Journal of Greenhouse Gas Control 63, 1-11, 2017 | 41 | 2017 |
Measurement of the viscosity and density of a reference fluid, with nominal viscosity at T= 298 K and p= 0.1 MPa of 29 mPa⊙ s, at temperatures between (273 and 423) K and … ME Kandil, KR Harris, ARH Goodwin, K Hsu, KN Marsh Journal of Chemical & Engineering Data 51 (6), 2185-2196, 2006 | 36 | 2006 |
Density and Viscosity of Diisodecyl Phthalate C6H4 (COOC10H21) 2, with Nominal Viscosity at T= 298 K and p= 0.1 MPa of 87 mPa⊙ s, at Temperatures from (298.15 to 423.15) K and … MM Al Motari, ME Kandil, KN Marsh, ARH Goodwin Journal of Chemical & Engineering Data 52 (4), 1233-1239, 2007 | 34 | 2007 |
Relative Permittivity of Dimethylsulfoxide and N,N-Dimethylformamide at Temperatures from (278 to 328) K and Pressures from (0.1 to 5) MPa J Hunger, R Buchner, ME Kandil, EF May, KN Marsh, G Hefter Journal of Chemical & Engineering Data 55 (5), 2055-2065, 2010 | 32 | 2010 |
Vapor− liquid equilibria measurements of the methane+ pentane and methane+ hexane systems at temperatures from (173 to 330) K and pressures to 14 MPa ME Kandil, MJ Thoma, T Syed, J Guo, BF Graham, KN Marsh, SH Huang, ... Journal of Chemical & Engineering Data 56 (12), 4301-4309, 2011 | 31 | 2011 |
Simulation and measurements of volumetric and phase behavior of carbon dioxide+ higher alkanes at high pressure: CO2+ n-decane at temperatures (313–410) K and pressures up to … ME Kandil, NM Al-Saifi, AS Sultan International Journal of Greenhouse Gas Control 53, 198-206, 2016 | 26 | 2016 |
Vapor− Liquid Equilibria Measurements of Methane+ 2-Methylpropane (Isobutane) at Temperatures from (150 to 250) K and Pressures to 9 MPa ME Kandil, EF May, BF Graham, KN Marsh, MA Trebble, RD Trengove, ... Journal of Chemical & Engineering Data 55 (8), 2725-2731, 2010 | 23 | 2010 |
Phase equilibrium measurements of (methane+ benzene) and (methane+ methylbenzene) at temperatures from (188 to 348) K and pressures to 13 MPa TJ Hughes, ME Kandil, BF Graham, KN Marsh, SH Huang, EF May The Journal of Chemical Thermodynamics 85, 141-147, 2015 | 22 | 2015 |
A re-entrant resonator for the measurement of phase boundaries: dew points for {0.4026 CH4+ 0.5974 C3H8} ME Kandil, KN Marsh, ARH Goodwin The Journal of Chemical Thermodynamics 37 (7), 684-691, 2005 | 21 | 2005 |
Determination of the Relative Permittivity, ϵ′, of Methylbenzene at Temperatures between (290 and 406) K and Pressures below 20 MPa with a Radio Frequency Re-Entrant Cavity … ME Kandil, KN Marsh, ARH Goodwin Journal of Chemical & Engineering Data 53 (5), 1056-1065, 2008 | 17 | 2008 |
Measurement of the viscosity of liquid cyclopentane obtained with a vibrating wire viscometer at temperatures between (273 and 353) K and pressures below 45 MPa K Kurihara, ME Kandil, KN Marsh, ARH Goodwin Journal of Chemical & Engineering Data 52 (3), 803-807, 2007 | 15 | 2007 |
The development of a vibrating wire viscometer and a microwave cavity resonator for the measurement of viscosity, dew points, density, and liquid volume fraction at high … ME Kandil University of Canterbury. Chemical and Process Engineering, 2005 | 15 | 2005 |
Determination of the relative permittivity and density within the gas phase and liquid volume fraction formed within the two-phase region for (0.4026 CH4+ 0.5974 C3H8) with a … ME Kandil, KN Marsh, ARH Goodwin Journal of Chemical & Engineering Data 52 (5), 1660-1671, 2007 | 14 | 2007 |
Simulating the capture of CO2 from natural gas: new data and improved models for methane+ carbon dioxide+ methanol TJ Hughes, ME Kandil, BF Graham, EF May International Journal of Greenhouse Gas Control 31, 121-127, 2014 | 11 | 2014 |
Evaluation of novel surfactant for nitrogen-foam-assisted eor in high salinity carbonate reservoirs AS Bageri, AS Sultan, ME Kandil SPE EOR Conference at Oil and Gas West Asia, SPE-169717-MS, 2014 | 11 | 2014 |
Measurements and Modeling of Phase Behavior, Density, and Viscosity of Oil + Carbon Dioxide: Squalane + CO2 at Temperatures 3 (313 to 363) K and Pressures up to 77 MPa ME Kandil Journal of Chemical and Engineering Data 64, 273-285, 2019 | 10 | 2019 |
Fluid Science for improved LNG Production and shipping EF May, G Watson, M Kandil, B Graham, T Hughes, P Arjomandnia, ... Presentation of the University Of Western Australia, 2010 | 6 | 2010 |