| 1 |
Effect of lifter shape and operating parameters on the flow of materials in a pilot rotary kiln: Part III. Up-scaling considerations and segregation analysis
Njeng ASB, Vitu S, Clausse M, Dirion JL, Debacq M
Powder Technology, 297, 415, 2016 |
| 2 |
Effect of lifter shape and operating parameters on the flow of materials in a pilot rotary kiln: Part I. Experimental RTD and axial dispersion study
Njeng ASB, Vitu S, Clausse M, Dirion JL, Debacq M
Powder Technology, 269, 554, 2015 |
| 3 |
Effect of lifter shape and operating parameters on the flow of materials in a pilot rotary kiln: Part II. Experimental hold-up and mean residence time modeling
Njeng ASB, Vitu S, Clausse M, Dirion JL, Debacq M
Powder Technology, 269, 566, 2015 |
| 4 |
A hydrodynamic model for flighted rotary kilns used for the conversion of cohesive uranium powders
Debacq M, Thammavong P, Vitu S, Ablitzer D, Houzelot JL, Patisson F
Chemical Engineering Science, 104, 586, 2013 |
| 5 |
Transverse motion of cohesive powders in flighted rotary kilns: experimental study of unloading at ambient and high temperatures
Debacq M, Vitu S, Ablitzer D, Houzelot JL, Patisson F
Powder Technology, 245, 56, 2013 |
| 6 |
Experimental Apparatus for Studying Heat Transfer in Externally Heated Rotary Kilns
Thammavong P, Debacq M, Vitu S, Dupoizat M
Chemical Engineering & Technology, 34(5), 707, 2011 |
| 7 |
Comments on "Solubility of CO(2), N(2), and CO(2)+N(2) Gas Mixtures in Isooctane" ( Zhang, J. S.; Lee, S.; Lee, J. W. J. Chem. Eng. Data 2008, 539 1321-1324)
Jaubert JN, Vitu S
Journal of Chemical and Engineering Data, 53(8), 2001, 2008 |
| 8 |
High-pressure phase behaviour of the binary system {CO2 + cis-decalin} from (292.75 to 373.75) K
Vitu S, Jaubert JN, Pauly J, Daridon JL
Journal of Chemical Thermodynamics, 40(9), 1358, 2008 |
| 9 |
Phase equilibria measurements of CO2+ methyl cyclopentane and CO2+ isopropyl cyclohexane binary mixtures at elevated pressures
Vitu S, Jaubert JN, Pauly J, Daridon JL, Barth D
Journal of Supercritical Fluids, 44(2), 155, 2008 |
| 10 |
Predicting the phase equilibria of CO2+ hydrocarbon systems with the PPR78 model (PR EOS and k(ij) calculated through a group contribution method)
Vitu S, Privat R, Jaubert JN, Mutelet F
Journal of Supercritical Fluids, 45(1), 1, 2008 |
