Aerobic and two-stage anaerobic–aerobic sludge digestion with pure oxygen and air aeration

2008 ◽  
Vol 99 (1) ◽  
pp. 100-109 ◽  
Author(s):  
Gregor D. Zupančič ◽  
Milenko Roš
2010 ◽  
Vol 22 (2) ◽  
pp. 230-236 ◽  
Author(s):  
Rohan Jain ◽  
Ashish Pathak ◽  
T.R. Sreekrishnan ◽  
M.G. Dastidar

1982 ◽  
Vol 16 (6) ◽  
pp. 1051-1060 ◽  
Author(s):  
Randolph M. Kabrick ◽  
William J. Jewell

2020 ◽  
Vol 167 ◽  
pp. 01010 ◽  
Author(s):  
Boonchai Wichitsathian ◽  
Jareeya Yimratanabovorn ◽  
Watcharapol Wonglertarak

The excess sludge problem from a wastewater treatment plant is a great concerned due to the high cost of sludge management accounting for about 20% to 50% of the total operating cost. Therefore, sludge reduction is critical. Currently, aerobic and/or anaerobic sludge digestions are widely used in the industries for treating the excess sludge. The objective of this research was to study the effects of aeration rate and temperature on the excess sludge reduction by using the aerobic-anaerobic digestion system in the laboratory. The aeration rates of 1.0, 0.5, and 0.1 volume air per volume slurry per minute (vvm) at the room temperature and the thermophilic temperature (55 ± 2°C) were investigated. The results showed that the highest removal efficiency of aerobic sludge digestion was obtained at the thermophilic temperature and aeration rate of 1.0 vvm. The removal efficiency of organic matter in terms of COD, total solids (TS) and volatile solids (VS) were 34.76%, 33.01% and 43.45%, respectively. Consequently, the highest specific growth rate of microorganisms was 0.39 per hour and the substrate removal rate was 0.55 milligram CODremoved per milligram VSS per hour. Furthermore, slowly biodegradable organic matter was hydrolyzed to readily biodegradable organic matter and inert soluble organic matter. When the sludge effluent from aerobic sludge digestion was feed to the anaerobic sludge digestion, the removal efficiency of organic matter in terms of COD, TS and VS were increased by 25%, 17% and 28%, respectively. Moreover, the obtained methane production rate in the anaerobic sludge digestion was approximate 0.234 m3/kg COD removed.


1986 ◽  
Vol 28 (11) ◽  
pp. 1699-1706 ◽  
Author(s):  
R. L. Droste ◽  
W. A. Sanchez

1973 ◽  
Vol 8 (1) ◽  
pp. 26-35
Author(s):  
K.S. Hogg ◽  
J. Ganczarczyk

Abstract The aerobic sludge digestion system at the sewage treatment plant at Dunnville, Ontario was designed as a one-stage aeration process (by means of the Inka system) of moderately concentrated excess activated sludge (less than 1 percent of TS), followed by continuous sludge thickening and sludge drying lagoons for the final dewatering of the digestion product. An evaluation of this system was conducted in the summer of 1972. It included the study of sludge and supernatant characteristics, phosphorus balance and an economical comparison of the costs associated with this type of aerobic digestion and anaerobic sludge digestion for similar size (about 1.7 IMGD) activated sludge process plants. Results of the investigations disclosed that the aerobic digester with sludge loading of about 0.03 lb VS/cu ft/day and an average hydraulic detention time of only 9.2 days, operated satisfactorily at the summer climatic conditions of Southern Ontario. This process, however, could not be judged on the basis of volatile solids reduction, which proved to be only equal to 6 percent. This phenomenon was probably due to the solubility in water of a part of the mineral constituents of the sludge under the process conditions. The change in the sludge specific oxygen uptake rates from 8.9 to 2.75 mg 02/gVSS/hr at 25°C, was a more reliable indicator of the digested sludge characteristics. Supernatant quality (average COD of 170 mg/l and SS of 110 mg/l) and the dewaterability of the digested sludge (average resistance to filtration equal to 0.86 x 1013 m/kg) provided additional information of the digester’s performance.


2008 ◽  
Vol 58 (6) ◽  
pp. 1237-1243
Author(s):  
Gregor D. Zupanèiè ◽  
Viktor Grilc ◽  
Milenko Roš ◽  
Nataša Uranjek-Ževart

An autothermal aerobic sequencing batch process for sludge digestion and “class A” biosolids production was developed. The process was tested in laboratory and pilot scale size up to 150 PE, which can be considered a full scale size in some cases. In this process the maximum temperatures of 61.2°C and 60.2°C were achieved in laboratory scale in pilot scale equipment, respectively. The degradation efficiency of total chemical oxygen demand of sludge was between 50 and 70%. Similar results were achieved using pure oxygen in laboratory scale and oxygen/air mixture 1:1 by volume. The reactor scale greatly affects the achievement of thermophilic temperature. In smaller sizes the convective heat losses are the prevailing heat sink and the process is unable to produce enough heat to reach thermophilic temperature. Larger systems produce excess heat and can be installed with less intense aeration systems. The limit of air aeration system is at the size of about 500 PE.


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