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Namely, the effect of aliasing terms in the low-pass subband has been approximately removed.
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Aquatic plant filter was the best at NH4 +-N removal and removed approximately 41.3% of the NH4 +-N load.
The oil water separator removed approximately 50% of the O & G, and removal extents and efficiencies approximated those observed at 50 mg L−1 inflow concentration during treatment without an oil water separator.
After enzymatic reaction for 120 min, almost all of the 25 mg kg−1 chlorothalonil on cherry tomatoes was removed, approximately 82% of the 45 mg kg−1 chlorothalonil on lactuca sativa was removed, and approximately 40%67%% of the chlorothalonil on all other vegetables was removed.
Additionally, the device removed approximately 87% of the protein from a cell lysate.
The intramedullary rods were removed approximately 1 year after the osteotomies.
Concrete sand removed approximately 93% of the soluble phosphorous in the wastewater and wollastonite, an economical aggregate alternative to sand, removed at least 98%.
A mass balance indicates that the swirl separator only removed approximately 23% of the total mass of TSS removed from this recirculating system.
The aeration cascades removed approximately 67% of the dissolved CO2 initially present but varying the design did not affect the concentration of Fe(II) leaving the treatment ponds.
In the batch-scale experiment, 2.5 mg L− 1 PAA removed approximately 4 log unit of E. coli and Enterococcus from CSO with a 360 min contact time.
Additionally, the aquatic plant filter was located in the main pool of phosphorus and removed approximately 58.4% of TP load and 68.4% of PO4 3−P load.
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