Biological Nutrient Removal using an IACOD Process: determining the Combined Effects of Low Temperature and Long Solids Retention Time

2006 ◽  
Vol 27 (5) ◽  
pp. 467-475 ◽  
Author(s):  
S. H. Lim ◽  
K. B. Ko ◽  
K. E. Rho
2012 ◽  
Vol 2012 ◽  
pp. 1-8 ◽  
Author(s):  
J. Sánchez Rubal ◽  
J. A. Cortacans Torre ◽  
I. del Castillo González

The aim of this research was to determine the influence of temperature, agitation, sludge concentration, and solids retention time (SRT) to obtain readily biodegradable organic matter on primary sludge (PS) fermentation, which would be used as substrate in a biological nutrient removal (BNR) process. Stirring and heating the sludge as well as increasing SRT improved the PS fermentation, producing a large amount of soluble chemical oxygen demand (SCOD). The influence of each operational parameter on PS hydrolysis was observed clearly. A great performance on SCOD production was obtained when the PS was stirred and heated for 3 days. However, PS concentration did not affect the fermentation. Sludge agitation is a simple process with minimal energy consumption. Warming the sludge is very interesting in those plants with anaerobic digestion, where heat energy is obtained from biogas. Therefore, PS fermentation can be improved with a minimum investment and leveraging existing resources in a wastewater treatment plant (WWTP). Fermenter volume can also be reduced if sludge is being heated and stirred during fermentation.


2016 ◽  
Vol 92 ◽  
pp. 44-51 ◽  
Author(s):  
Halis Simsek ◽  
Murthy Kasi ◽  
Jae-Bom Ohm ◽  
Sudhir Murthy ◽  
Eakalak Khan

1994 ◽  
Vol 30 (6) ◽  
pp. 101-111 ◽  
Author(s):  
H. Siegrist ◽  
W. Gujer

Denitrification in the secondary clarifier can contribute substantially to the nitrogen removal of activated sludge systems. This is illustrated on two treatment plants with different secondary clarifier systems. A model to estimate denitrification capacity and to design activated sludge systems for nitrogen removal is developed and verified with data from two treatment plants. The model includes denitrification in the secondary clarifier, wastewater composition (soluble readily biodegradable COD, particulate degradable COD), oxygen input into the anoxic volume, temperature, and solids retention time (SRT). The influence of aerated grit chambers and primary sedimentation on denitrification is discussed.


2005 ◽  
pp. 61-69
Author(s):  
Koji HAMADA ◽  
Takahiro KUBA ◽  
Mitsuo OKAZAKI ◽  
Vladimir TORRICO ◽  
Tetsuya KUSUDA

Water SA ◽  
2007 ◽  
Vol 32 (3) ◽  
Author(s):  
C Noutsopoulos ◽  
D Mamais ◽  
A Andreadakis

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