Influence of non-conducting suspended solids onto the efficiency of electrochemical reactors using fluidized bed electrodes

2021 ◽  
pp. 130322
Author(s):  
André Tschöpe ◽  
Matthias Franzreb
1994 ◽  
Vol 30 (11) ◽  
pp. 101-110
Author(s):  
Toshiaki Tsubone ◽  
Seiichi Kanamori ◽  
Tatsuo Takechi ◽  
Masahiro Takahashi

A pilot scale study was conducted using an Air-Fluidized-Bed Biofilm Reactor (AFBBR) system with a Multi Media Filter (MMF). Soluble BOD (S-BOD) concentration in the effluent of the AFBBR had a correlation with total BOD (T-BOD) and Suspended Solids (SS) concentration in the effluent of the MMF. The lower the S-BOD in the effluent of the AFBBR was, the lower was not only T-BOD but also SS in the effluent of the MMF. It was found that as treatment proceeded, S-BOD was removed and the particle size of SS increased in the AFBBR. These results suggested that the mechanism of BOD removal in this system was: S-BOD was removed and a part of the S-BOD was changed to SS and the particle size of the SS increased in the AFBBR, and then the SS was removed by the MMF. Thus not only the T-BOD but also the SS in the effluent of MMF was lower when the S-BOD in the effluent of the AFBBR was lower. When the S-BOD in the effluent of the AFBBR was 8mg/L, T-BOD and the SS in the effluent of the MMF were 10mg/L and 4mg/L, respectively. In order to have an average S-BOD value in the effluent of the AFBBR of about 8mg/L, the T-BOD loading and the S-BOD loading needed to be less than 1.3kg/m3/day and 0.45 kg/m3/day, respectively. Even when the BOD loading was high, nitrification still occurred in this system.


2000 ◽  
Vol 41 (4-5) ◽  
pp. 245-251 ◽  
Author(s):  
P. Castilla ◽  
M. Meraz ◽  
O. Monroy ◽  
A. Noyola

Low concentration synthetic and municipal wastewaters were treated at HRT as short as 3 and 0.6 h respectively in an anaerobic inverse fluidized bed. Both bioreactors showed gas hold up due to the liquid downflow pattern of the prototype. The bioreactor operated at 3 h had a removal efficiency of 83%, specific activity of 4.5 kg CODremoved/kg IVS (d and the gas hold up varied from 23 to 55%. The reactor treating municipal wastewater had a removal efficiency of 44% when operating at 0.6 h, the specific activity was 4.2 kg CODremoved/kg IVS (d and no biogas was detected apparently because an important fraction was dissolved in the liquid phase. The biomass concentration was 13.8 and 1.1 kg IVS/m3 for synthetic and municipal wastewater and the SEM microphotographs showed a bacterial diversity for the first run and only cocci cells for the second run. The system does not remove suspended solids, so a polishing postreatment to improve water quality has to be implemented.


1991 ◽  
Vol 23 (7-9) ◽  
pp. 1695-1702 ◽  
Author(s):  
S. Elmaleh ◽  
J. Coma ◽  
A. Grasmick ◽  
L. Bourgade

The effectiveness of the use of seawater and of magnesium in the removal of microalgae from oxidation pond effluents was investigated using the jar test procedure. The results indicated that the major flocculating reaction is the magnesium hydroxide precipitation at pH 11.5. The next step was to intensify the liquid-solids separation by use of a fluidized bed flocculator packed with 800 µm inert resin particles provided with an inclined multitubular settler. The total suspended solids abatement could reach 95 % with a superficial upflow velocity of 30 m/h corresponding to a residence time through the whole unit of 5 minutes only. The energy requirement quantified by the pressure drop through the bed is very low. Besides, the waste sludge extracted from the settler is easily thickened.


1992 ◽  
Vol 26 (7-8) ◽  
pp. 1689-1696 ◽  
Author(s):  
S. Elmaleh ◽  
J. Coma ◽  
J. Borsato

The effectiveness of the microalgae flocculation by a fluidized bed of magnesium exchanger resin particles was investigated. The results indicated that the total suspended solids abatement could reach 90% at pH 11.5 while the superficial upflow velocity was 30 m/h which corresponds to a residence time through the flocculator less than 1 minute. The abatement remains steady even after exhaustion of the ion exchange capacity while the bed is continuously expanding which makes the resin regeneration easy and lowers the magnesium requirement. The extracted sludge is easily thickened. The destabilized suspension is itself easily concentrated by sedimentation followed by single draining.


1991 ◽  
Vol 24 (7) ◽  
pp. 217-222 ◽  
Author(s):  
J. Coma ◽  
A. Jabbouri ◽  
A. Grasmick ◽  
S. Elmaleh

The intensification of primary treatment is basically obtained by destabilization through a fluidized bed which flocculates the suspension with or even without any flocculant. The abatement on suspended solids reaches 60 % in the latter case, and rises up to 90% when ferric chloride is injected. The required residence-time in the whole unit is only 15 minutes, settling included. The sludge has a better settling ability than sludge from classical devices which could reduce the cost of the sludge treatment itself.


2000 ◽  
Vol 79 (3) ◽  
pp. 203-209 ◽  
Author(s):  
K Kazdobin ◽  
N Shvab ◽  
S Tsapakh

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