Characterization of microbial populations in pilot-scale fluidized-bed reactors treating perchlorate- and nitrate-laden brine

2010 ◽  
Vol 44 (14) ◽  
pp. 4029-4036 ◽  
Author(s):  
Yeyuan Xiao ◽  
Deborah J. Roberts ◽  
Geyan Zuo ◽  
Mohammad Badruzzaman ◽  
Geno. S. Lehman
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.


1981 ◽  
Vol 10 (4-5) ◽  
pp. 307-330 ◽  
Author(s):  
D. WIPPERN ◽  
K. WITTMANN ◽  
J. KÜHNE ◽  
H. HELMRICH ◽  
K. SCHÜGERL

Energy ◽  
2018 ◽  
Vol 151 ◽  
pp. 520-535 ◽  
Author(s):  
J. Cardoso ◽  
V. Silva ◽  
D. Eusébio ◽  
P. Brito ◽  
M.J. Hall ◽  
...  

1994 ◽  
Vol 29 (10-11) ◽  
pp. 353-360 ◽  
Author(s):  
I. Ozturk ◽  
M. Turan ◽  
A. H. Idris

This paper presents a comprehensive study results on scale-up and biomass hold-up characteristics of biological fluidized bed reactors (BFBR). The overall objective of this study was to establish and test some basic design criteria for the scaling-up or scaling-down of anaerobic fluidized bed reactors. A 12.5 1 laboratory-scale fluidized bed was designed and constructed based on a geometrically similar 70 1 pilot scale fluidized bed and the process performances were compared. Biomass hold up characteristics of the BFBRs were also investigated during the experimental studies. A general expression was developed for predicting the biological fludized bed porosities. Using this expression, both the local and overall fluidized bed porosities could be predicted depending on biofilm thickness, expansion coefficient, media diameter and density. The validity of this expression was tested with the data from this study.


2011 ◽  
Vol 102 (4) ◽  
pp. 3840-3847 ◽  
Author(s):  
Aruana Rocha Barros ◽  
Maria Angela Tallarico Adorno ◽  
Isabel Kimiko Sakamoto ◽  
Sandra Imaculada Maintinguer ◽  
Maria Bernadete Amâncio Varesche ◽  
...  

2011 ◽  
Vol 88 (9) ◽  
pp. 2940-2948 ◽  
Author(s):  
Yinghai Wu ◽  
Chunbo Wang ◽  
Yewen Tan ◽  
Lufei Jia ◽  
Edward J. Anthony

2010 ◽  
Vol 156 (1) ◽  
pp. 170-176 ◽  
Author(s):  
J.L. Pinilla ◽  
M.J. Lázaro ◽  
I. Suelves ◽  
R. Moliner ◽  
J.M. Palacios

Processes ◽  
2021 ◽  
Vol 9 (2) ◽  
pp. 279
Author(s):  
Alberto Di Renzo ◽  
Erasmo Napolitano ◽  
Francesco Di Maio

In the last decade, a few of the early attempts to bring CFD-DEM of fluidized beds beyond the limits of small, lab-scale units to larger scale systems have become popular. The simulation capabilities of the Discrete Element Method in multiphase flow and fluidized beds have largely benefitted by the improvements offered by coarse graining approaches. In fact, the number of real particles that can be simulated increases to the point that pilot-scale and some industrially relevant systems become approachable. Methodologically, coarse graining procedures have been introduced by various groups, resting on different physical backgrounds. The present review collects the most relevant contributions, critically proposing them within a unique, consistent framework for the derivations and nomenclature. Scaling for the contact forces, with the linear and Hertz-based approaches, for the hydrodynamic and cohesive forces is illustrated and discussed. The orders of magnitude computational savings are quantified as a function of the coarse graining degree. An overview of the recent applications in bubbling, spouted beds and circulating fluidized bed reactors is presented. Finally, new scaling, recent extensions and promising future directions are discussed in perspective. In addition to providing a compact compendium of the essential aspects, the review aims at stimulating further efforts in this promising field.


2014 ◽  
Author(s):  
Michelle H. Lee ◽  
Sabrina D. Saurey ◽  
Brady D. Lee ◽  
Kent E. Parker ◽  
Emalee E. R. Eisenhauer ◽  
...  

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