A downflow denitrification filter making by sand medium is designed for feeding
ID: 998337 • Letter: A
Question
A downflow denitrification filter making by sand medium is designed for feeding with secondary effluent to achieve effluent TSS and NO3-N concentrations less than 5.0 and 2.0 mg/L respectively. At 15oC operation, the NO3-N loading into filter is selected at 1.3 kg/m3day and the filter depth is 1.5m.
Given that with the following wastewater characteristics: Flowrate = 7000 m3 /day TSS = 25 g/m3 NO3-N = 20 g/m3 Temperature = 15oC
(i) Determine the filter size dimension based on the NO3-N loading (assumed it is a square type filter)
(ii) Determine the total amount of solids being trapped by this filter (assumed the total amount of solids is contributed from only 2 parts, i.e. filtered TSS and the active biomass growing under the methanol (CH3OH) addition):
Parameters given: Synthesis yield with methanol = 0.18g VSS/g CODutilized VSS/TSS =0.85 g COD/g CH3OH = 1.5 g CH3OH /g NO3-N = 3.2
Explanation / Answer
A]Flowrate = 7000 m3 /day
TSS = 25 g/m3
NO3-N = 20 g/m3
Temperature = 15oC
filter depth is 1.5m
.Synthesis yield with methanol = 0.18g VSS/g
VSS/TSS =0.85 g COD/g
CH3OH = 1.5 g CH3OH /g
NO3-N removal=[ (25-2.0)g/m3*(7000m^3/d (1kg/10^3)}
=161kg/d.
the NO3-N loading at 15 degrees C is 1.3 kg/m3day and the D depth is 1.5m.
Volume={161kg/d.} /1.3kg/m3.d
=123.8m3.
AREA=volumedepth
=123.8m3./1.5m
=82.5m2.
square dimensions=82.5m2
=20.6m2
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