Infiltration Behavior of Microplastic Particles with Different Densities, Sizes, and Shapes—From Glass Spheres to Natural Sediments

2020 ◽  
Vol 54 (15) ◽  
pp. 9366-9373 ◽  
Author(s):  
Kryss Waldschläger ◽  
Holger Schüttrumpf
1973 ◽  
Vol 43 (2) ◽  
pp. 350-369 ◽  
Author(s):  
Joseph A Fitzpatrick ◽  
Lloyd A Spielman
Keyword(s):  

1996 ◽  
Vol 36 (18) ◽  
pp. 2352-2365 ◽  
Author(s):  
H. R. Azimi ◽  
R. A. Pearson ◽  
R. W. Hertzberg

2007 ◽  
Vol 22 (8) ◽  
pp. 2273-2278 ◽  
Author(s):  
J.M. Molina ◽  
J. Tian ◽  
C. Garcia-Cordovilla ◽  
E. Louis ◽  
J. Narciso

The infiltration behavior of compacts of SiC particles in two surface conditions, as-received and thermally oxidized, was investigated by using pure Al and Al-12wt%Si as infiltrating metals. Analysis of the threshold pressure for infiltration revealed that the process is governed by the same contact angle for all different systems, no matter the metal or particle condition. This leads to the conclusion that oxidation does not modify the wetting characteristics of the particles, most probably because they are already covered by a thin native oxide layer that remains unaltered in processing routes involving short contact times and low temperatures, such as actual conditions of pressure infiltration at 700 °C.


1967 ◽  
Vol 166 (1) ◽  
pp. 59-64 ◽  
Author(s):  
MICHAEL HUME
Keyword(s):  

2011 ◽  
Author(s):  
Pål Løvhaugen ◽  
Balpreet S. Ahluwalia ◽  
Olav G. Hellesø

Author(s):  
Kyla Clarke ◽  
Gordon A Hill ◽  
Todd S. Pugsley

A gas-solid fluidized bed bioreactor has been successfully used for the bioremediation of ethanol (a model volatile organic compound, VOC) contaminated air. A key objective of this fluidized bioreactor study was to compare the performance of fluid bed operation to packed bed operation. A fluid bed system increased homogeneity and improved upon operating problems such as plugging and channelling normally associated with packed bed bioreactors. The bioreactor bed was comprised of a mixture of moist sawdust particles and glass spheres. Depending on the superficial velocity of the waste gas stream, the bioreactor could be operated in either packed or fluidized mode. During fluid bed operation, the sawdust and glass sphere mixture was maintained in a bubbling/slugging regime. As expected, fluid bed operation demonstrated significantly higher mass transfer rates but the maximum elimination capacity was 75 g m-3sawdust h-1 as compared to 225 g m-3sawdust h-1 for packed bed operation. In packed bed mode, higher ethanol concentrations were used in order to have comparable ethanol loadings and this may have contributed to faster growth rates and thus faster bioremediation rates.


2021 ◽  
pp. 117081
Author(s):  
Chunhe Miao ◽  
Songlin Xu ◽  
Yiping Song ◽  
Yushan Xie ◽  
Liangzhu Yuan ◽  
...  

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