| 809 - 814 |
Zeolite nanocrystals prepared from zeolite microparticles by a centrifugation-assisted grinding method
Kong CL, Tsuru T |
| 815 - 819 |
Wet air oxidation of polyether solutions
Tang WW, Zeng XP, Wang QA, Li P |
| 820 - 824 |
Gas-side mass transfer coefficients in a falling film microreactor
Sobieszuk P, Pohorecki R |
| 825 - 835 |
Design and optimization of a dividing wall column for debottlenecking of the acetic acid purification process
Long NVD, Lee S, Lee M |
| 836 - 842 |
Effect of process conditions on particle growth for spouted bed coating of urea
da Rosa GS, Rocha SCD |
| 843 - 851 |
An engineering model of a gas bubble-liquid turbulent flow in coiled tubing wound on a reel
Eskin D |
| 852 - 858 |
Interfacial area and mass transfer in carbon dioxide absorption in TEA aqueous solutions in a bubble column reactor
La Rubia MD, Garcia-Abuin A, Gomez-Diaz D, Navaza JM |
| 859 - 865 |
Flue gas desulfurization by FeSO4 solutions and coagulation performance of the polymeric ferric sulfate by-product
Zhang Y, Guo SY, Zhou JT, Li CY, Wang GD |
| 866 - 872 |
Supercritical extraction of grape seed oil at industrial-scale: Plant and process design, modeling, economic feasibility
Fiori L |
| 873 - 880 |
Catalytic cracking of rapeseed oil to high octane gasoline and olefins
Bielansky P, Reichhold A, Schonberger C |
| 881 - 884 |
A modification of the Pr value equation for measuring the compactibility of pharmaceutical materials
Ilic I, Kasa P, Dreu R, Pintye-Hodi K, Srcic S |
