Absorption of hydrogen by amorphous and crystalline 89Fe-11P powder: deformation of the powder under pressure and relaxation on heating

1996 ◽  
Vol 45 (3) ◽  
pp. 280-283 ◽  
Author(s):  
D.M. Minić ◽  
M.V. Šušić ◽  
A.M. Maričić
2012 ◽  
Vol 137 (8) ◽  
pp. 084509 ◽  
Author(s):  
W. A. Herrebout ◽  
B. J. van der Veken ◽  
A. P. Kouzov

1956 ◽  
Vol 77 (2) ◽  
pp. 295-297
Author(s):  
Toshizo Titani ◽  
Yoshihide Naito ◽  
Atsuo Konishi

2006 ◽  
Vol 47 (20) ◽  
pp. 3632-3643 ◽  
Author(s):  
Philippe Marty ◽  
J.-F. Fourmigue ◽  
P. De Rango ◽  
D. Fruchart ◽  
J. Charbonnier

Langmuir ◽  
1993 ◽  
Vol 9 (4) ◽  
pp. 984-992 ◽  
Author(s):  
R. W. Wunder ◽  
J. W. Cobes ◽  
J. Phillips ◽  
L. R. Radovic ◽  
A. J. Lopez Peinado ◽  
...  

Processes ◽  
2018 ◽  
Vol 6 (8) ◽  
pp. 117 ◽  
Author(s):  
Nassima Benamara ◽  
Didier Assoua ◽  
Louis Jaffeux ◽  
Laurent Vanoye ◽  
Florica Simescu-Lazar ◽  
...  

Developing new stirred gas–liquid–solid reactors with high mass transfer capabilities is still a challenge. In this publication, we present a new concept of multiphase reactor using a stationary catalytic foam and a gas-inducing impeller. The gas–liquid (GL) and liquid–solid (LS) mass transfer rates in this reactor were compared to a stirred reactor with basket filled with beads. Batch absorption of hydrogen and measurement of α-methylstyrene hydrogenation rate on Pd/Al2O3 catalyst were used to evaluate kGLaGL coefficients and kLS coefficients, respectively. With similar LS transfer rates to the basket-reactor and much higher GL transfer rates, the new reactor reveals a very promising tool for intrinsic kinetics investigations.


1991 ◽  
Vol 172-174 ◽  
pp. 64-70 ◽  
Author(s):  
A. Kagawa ◽  
E. Ono ◽  
T. Kusakabe ◽  
Y. Sakamoto

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