| 1 |
A new methodology for the production of furfural as a renewable energy source from bagasse in acidic aqueous media
Yazdizadeh M, Nasr MRJ, Safekordi AK
Energy Sources Part A-recovery Utilization and Environmental Effects, 40(2), 125, 2018 |
| 2 |
Applications of cubic equations of state for determination of the solubilities of industrial solid compounds in supercritical carbon dioxide: A comparative study
Yazdizadeh M, Eslamimanesh A, Esmaeilzadeh F
Chemical Engineering Science, 71, 283, 2012 |
| 3 |
Gas Hydrate Phase Equilibrium in Porous Media: Mathematical Modeling and Correlation
Mohammadi AH, Eslamimanesh A, Richon D, Gharagheizi F, Yazdizadeh M, Javanmardi J, Hashemi H, Zarifi M, Babaee S
Industrial & Engineering Chemistry Research, 51(2), 1067, 2012 |
| 4 |
Chrastil-Type Approach for Representation of Glycol Loss in Gaseous System
Eslamimanesh A, Mohammadi AH, Yazdizadeh M, Richon D
Industrial & Engineering Chemistry Research, 50(17), 10373, 2011 |
| 5 |
Phase Equilibrium Modeling of Structure H Clathrate Hydrates of Methane plus Water "Insoluble" Hydrocarbon Promoter Using Group Contribution-Support Vector Machine Technique
Eslamimanesh A, Gharagheizi F, Mohammadi AH, Richon D, Illbeigi M, Fazlali A, Forghani AA, Yazdizadeh M
Industrial & Engineering Chemistry Research, 50(22), 12807, 2011 |
| 6 |
Experimental Data Assessment Test for Diamondoids Solubility in Gaseous System
Eslamimanesh A, Yazdizadeh M, Mohammadi AH, Richon D
Journal of Chemical and Engineering Data, 56(5), 2655, 2011 |
| 7 |
Glycol Loss in a Gaseous System: Thermodynamic Assessment Test of Experimental Solubility Data
Mohammadi AH, Eslamimanesh A, Yazdizadeh M, Richon D
Journal of Chemical and Engineering Data, 56(11), 4012, 2011 |
| 8 |
Thermodynamic modeling of solubilities of various solid compounds in supercritical carbon dioxide: Effects of equations of state and mixing rules
Yazdizadeh M, Eslamimanesh A, Esmaeilzadeh F
Journal of Supercritical Fluids, 55(3), 861, 2011 |
| 9 |
Thermodynamic modeling of CO2 solubility in ionic liquid ([C(n)-mim] [Tf2N]; n=2, 4, 6, 8) with using Wong-Sandler mixing rule, Peng-Rabinson equation of state (EOS) and differential evolution (DE) method
Yazdizadeh M, Rahmani F, Forghani AA
Korean Journal of Chemical Engineering, 28(1), 246, 2011 |
