Application of the bio-inspired Krill Herd optimization technique to phase equilibrium calculations K Moodley, J Rarey, D Ramjugernath Computers & Chemical Engineering 74, 75-88, 2015 | 31 | 2015 |
Model evaluation for the prediction of solubility of active pharmaceutical ingredients (APIs) to guide solid–liquid separator design K Moodley, J Rarey, D Ramjugernath asian journal of pharmaceutical sciences 13 (3), 265-278, 2018 | 21 | 2018 |
Improvement of the learning and assessment of the practical component of a Process Dynamics and Control course for fourth year chemical engineering students K Moodley Education for Chemical Engineers 31, 1-10, 2020 | 16 | 2020 |
Identification and screening of potential organic solvents for the liquid–liquid extraction of aromatics N Brijmohan, K Moodley, C Narasigadu Organic Process Research & Development 25 (10), 2230-2248, 2021 | 14 | 2021 |
Isothermal vapor–liquid equilibrium measurements for the pentan-2-one+ propan-1-ol/butan-1-ol system within 342–363 K S Mavalal, T Chetty, K Moodley Journal of Chemical & Engineering Data 64 (6), 2649-2656, 2019 | 13 | 2019 |
Experimental solubility for betulin and estrone in various solvents within the temperature range T=(293.2 to 328.2) K K Moodley, J Rarey, D Ramjugernath The Journal of Chemical Thermodynamics 98, 42-50, 2016 | 13 | 2016 |
P–ρ–T Data and Modeling for Propan-1-ol + n-Octane or n-Nonane or n-Decane from 313.15 K to 363.15 K and 1 MPa to 20 MPa K Moodley, S Adam, P Naidoo, S Naidu, D Ramjugernath Journal of Chemical & Engineering Data 63 (11), 4136-4156, 2018 | 12 | 2018 |
Experimental solubility of diosgenin and estriol in various solvents between T=(293.2–328.2) K K Moodley, J Rarey, D Ramjugernath The Journal of Chemical Thermodynamics 106, 199-207, 2017 | 11 | 2017 |
Isothermal vapour-liquid equilibrium measurements for the water+ butane-1, 4-diol/butane-2, 3-diol system within 353.1–373.2 K S Mavalal, K Moodley Fluid Phase Equilibria 512, 112518, 2020 | 9 | 2020 |
P–ρ–T Data and Modeling for Butan-1-ol + n-Octane or n-Decane between 313.15–353.15 K and 0.1–20 MPa M Hussain, K Moodley Journal of Chemical & Engineering Data 65 (4), 1636-1654, 2020 | 9 | 2020 |
Isothermal Vapor–Liquid Equilibrium Measurements of Butan-2-one+ 2-Methyl-propan-1-ol/Pentan-1-ol K Moodley, CL Dorsamy Journal of Chemical & Engineering Data 63 (11), 4128-4135, 2018 | 9 | 2018 |
Ternary Liquid–Liquid Equilibrium Data for the n-Heptane + Toluene + (Butane-1,4-diol or Glycerol) Systems at 298.2, 313.2, and 333.2 K and 0.1 MPa N Brijmohan, K Moodley, C Narasigadu Journal of Chemical & Engineering Data 67 (4), 975-983, 2022 | 7 | 2022 |
Vapor–Liquid Equilibrium Data for the Morpholine-4-carbaldehyde + n-Hexane or n-Heptane Binary Systems Using a Static-Synthetic Apparatus K Moodley, P Naidoo, JD Raal, D Ramjugernath Journal of Chemical & Engineering Data 58 (9), 2552-2566, 2013 | 7 | 2013 |
Liquid–Liquid Extraction of Toluene from n-Heptane Using Butane-1,4-diol + 2-Methyl-pentane-2,4-diol Liquid Mixtures N Brijmohan, K Moodley, C Narasigadu Journal of Chemical & Engineering Data 67 (10), 3177-3185, 2022 | 5 | 2022 |
P–T–x Measurement and Modeling of Methane or Carbon Dioxide + Methanol +2,2′-[Ethane-1,2-diylbis(oxy)] di(ethan-1-ol) Systems from T = 298 to 323 K P Zvawanda, P Naidoo, WM Nelson, K Moodley Journal of Chemical & Engineering Data 67 (5), 1174-1187, 2022 | 5 | 2022 |
P-ρ-T data and modelling for (2-methylpropan-1-ol+ n-octane or n-decane) between 313.15 K–353.15 K and 0.1–20 MPa M Hussain, K Moodley The Journal of Chemical Thermodynamics 152, 106279, 2021 | 5 | 2021 |
Solid–Liquid Equilibrium Measurements for Posaconazole and Voriconazole in Several Solvents between T = 278.2 and 323.2 K Using Differential Thermal … K Moodley, T Chetty, D Ramjugernath Journal of Chemical & Engineering Data 64 (8), 3367-3374, 2019 | 5 | 2019 |
Isothermal Vapor–Liquid Equilibrium Measurements for Alcohol + Water/n-Hexane Azeotropic Systems Using Both Dynamic and Automated Static-Synthetic Methods K Moodley, P Naidoo, JD Raal, D Ramjugernath Journal of Chemical & Engineering Data 64 (6), 2657-2670, 2019 | 5 | 2019 |
Excess Properties and Phase Equilibria for the Potential Biofuel System of Propan-2-ol and 2-Methyl-propan-1-ol at 333.15, 343.15, and 353.15 K K Moodley, CL Dorsamy, C Narasigadu, Y Vemblanathan Journal of Chemical & Engineering Data 63 (6), 2106-2113, 2018 | 5 | 2018 |
Experimental solubility data for prednisolone and hydrocortisone in various solvents between (293.2 and 328.2) K by employing combined DTA/TGA K Moodley, J Rarey, D Ramjugernath Journal of Molecular Liquids 240, 303-312, 2017 | 5 | 2017 |