Development and Scale-Up of an Aerobic Biofilm Air-Lift Suspension Reactor

1993 ◽  
Vol 27 (5-6) ◽  
pp. 253-261 ◽  
Author(s):  
J. J. Heijnen ◽  
M. C. M. van Loosdrecht ◽  
R. Mulder ◽  
R. Weltevrede ◽  
A. Mulder

A new aerobic treatment concept for the aerobic oxidation of COD, ammonia and sulphide has been developed. The concept is based on the formation of biofilms on small suspended particles in an air-lift reactor. This reactor concept enables to combine a low sludge loading with a high volumetric loading. This makes the reactor especially useful for e.g. nitrification processes. It is also feasible to operate under conditions of marginal sludge production. In this article the scale up aspects of such a process are discussed.

2007 ◽  
Vol 22 (3) ◽  
pp. 447-458
Author(s):  
Urszula Filipkowska ◽  
Aneta Hołownia-Kosak

2012 ◽  
Vol 84 ◽  
pp. 138-146 ◽  
Author(s):  
Yan Wang ◽  
Hui Zhang ◽  
Lu Chen ◽  
Sheng Wang ◽  
Daobin Zhang
Keyword(s):  

2008 ◽  
Vol 138 (1-3) ◽  
pp. 231-238 ◽  
Author(s):  
Hui Zhang ◽  
Yujuan Lv ◽  
Fang Liu ◽  
Daobin Zhang

Author(s):  
Marie DUQUESNE ◽  
Elena PALOMO DEL BARRIO ◽  
Alexandre GODIN

Xylitol is an organic, non-toxic, biosourced phase change material with high potential for seasonal thermal energy storage material. It has a high energy density, a high and stable undercooling allowing storing solar energy at ambient temperature thus, reducing thermal losses and the risk of spontaneous nucleation (i.e., the risk of losing the stored energy). When the energy is needed, the discharge triggering of the storage system (i.e., Nucleation triggering of highly viscous undercooled Xylitol) is very difficult as well as reaching a sufficient power delivery (i.e., the control of the subsequent crystal growth rates). Both are the mains locks for the use of Xylitol in seasonal energy storage. Different techniques to crystallize highly undercooled Xylitol have hence been considered. It has been proven that nucleation triggering of highly undercooled Xylitol using an air lift reactor would allow reaching performances matching with building applications (i.e., at medium temperatures, below 100 °C). The advantages of this technique compared to other existing techniques to activate the crystallization are discussed. The mechanisms triggering the nucleation are investigated. The air bubble generation, transportation of nucleation sites and subsequent crystallization are discussed to improve the air injection operating conditions.


1990 ◽  
Vol 22 (12) ◽  
pp. 229-238 ◽  
Author(s):  
R. D. Tyagi ◽  
D. Couillard ◽  
F. T. Tran

A comparative study between continuous stirred tank reactor (CSTR) with cell recycle and air-lift reactor was carried out in 30 1 capacity reactors for metal solubilization from anaerobically digested sludge. In CSTR at a residence time of 0.75 day, supplementing the feed sludge with 4 g/l of FeSO4.7H2O, using 20% sludge recycle and adjusting pH of the feed sludge to 4.5 resulted in following metal solubilization : 91% Cu, 94% Zn,, 93% Mn, 67% Cd, 67% Ni, 8% Cr, and 7% Pb. At 0.75 day retention time metals were solubilized to the recommended level in CSTR as well as in air-lift reactor. The treated sludge is easy to filter in plates filter press, centrifugation, or vacuum filter. The sludge nutrients do not seem to be diminished as a result of treatment and separation of solid-liquid. The ammonia-nitrogen fraction seems to be transformed in organic nitrogen. The decontaminated sludge produced has less odour.


1992 ◽  
Vol 26 (3-4) ◽  
pp. 647-654 ◽  
Author(s):  
J. J. Heijnen ◽  
M. C. M. van Loosdrecht ◽  
A. Mulder ◽  
L. Tijhuis

Biofilm Air-lift Suspension reactors can be used to treat waste water at a high volumetric loading rate combined with a low sludge loading. The biofilms are formed on small suspended particles (r = 0.1 mm). We have studied the effect of particle characteristics and hydraulic retention time on the biofilm formation. It is shown that small, rough particles show the best biofilm formation. Low hydraulic retention times benefit the formation of biofilms. This results from the fact that suspension growth is minimal under these conditions. The effect of biofilm detachment became distinct from the observation that most of the bacterial growth in the biofilm is transferred to the liquid. The biofilm formation process is concluded to be a three stage process: (i) the outgrowth of single cells to micro-colonies, this process is positively influenced by the carrier surface roughness; (ii) the outgrowth of micro-colonies to small biofilms, this process is negatively influenced by the concentration of carrier material; (iii) the outgrowth of biofilms, this occurs when the majority of particles are covered with a biofilm. At that time the influence of shear due to particle-particle interactions diminishes.


2011 ◽  
Vol 5 (4) ◽  
pp. 455-462 ◽  
Author(s):  
Mona Ebrahimifakhar ◽  
Elmira Mohsenzadeh ◽  
Sadegh Moradi ◽  
Mostafa Moraveji ◽  
Mahmoud Salimi

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