Functionalization of polymer powders for SLS-processes using an atmospheric plasma jet in a fluidized bed reactor

Author(s):  
Marius Sachs ◽  
Adeliene Schmitt ◽  
Jochen Schmidt ◽  
Wolfgang Peukert ◽  
Karl-Ernst Wirth
2018 ◽  
Vol 325 ◽  
pp. 490-497 ◽  
Author(s):  
Marius Sachs ◽  
Jochen Schmidt ◽  
Wolfgang Peukert ◽  
Karl-Ernst Wirth

2004 ◽  
Vol 2 (1) ◽  
pp. 38-44 ◽  
Author(s):  
Michaël Tatoulian ◽  
Frédéric Brétagnol ◽  
Farzaneh Arefi-Khonsari ◽  
Jacques Amouroux ◽  
Otman Bouloussa ◽  
...  

1997 ◽  
Vol 88 (1-3) ◽  
pp. 226-231 ◽  
Author(s):  
Takanobu Hanabusa ◽  
Shigeyuki Uemiya ◽  
Toshinori Kojima

2004 ◽  
Vol 4 (5-6) ◽  
pp. 21-28
Author(s):  
S.-C. Kim ◽  
D.-K. Lee

TiO2-coated granular activated carbon was employed for the removal of toxic microcystin-LR from water. High surface area of the activated carbon provided sites for the adsorption of microcystin-LR, and the adsorbed microcystin-LR migrated continuously onto the surface of TiO2 particles which located mainly at the exterior surface in the vicinity of the entrances of the macropores of the activated carbon. The migrated microcystin-LR was finally degraded into nontoxic products and CO2 very quickly. These combined roles of the activated carbon and TiO2 showed a synergistic effect on the efficient degradation of toxic microcystin-LR. A continuous flow fluidized bed reactor with the TiO2-coated activated carbon could successfully be employed for the efficient photocatalytic of microcystin-LR.


1989 ◽  
Vol 21 (4-5) ◽  
pp. 157-165 ◽  
Author(s):  
F. Ehlinger ◽  
J. M. Audic ◽  
G. M. Faup

The characterization of the biofilm of an anaerobic fluidized-bed reactor was completed under standard conditions. The distribution of the fixed protein concentration depended on the level in the reactor. The protein concentration reached 1520 µg.g−1 of support at the top of the reactor and only 1200 µg.g−1 at the bottom after 504 hours of operation but the specific activity of the biofilm was 33×10−4 µM acetate.h−1.mg−1 proteins at the bottom and only 26×10−4 µM.h−1.mg−1 at the top. The efficiency of a fluidized bed reactor and the composition of the biofilm changed with an increase of the pH from 7 to 8.5 during the seeding of the support material. Future development of the biofilm and the specific activity of the support were affected.


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