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The effluent air was dried over silica gel and a fraction of the dry effluent air was directed into the oxygen analyser.
Dry effluent from reactors was plumbed to a 16-position switching valve (VICI Valco Instruments, Houston, TX ., which switched positions every 20 min as controlled by a personal computer running LabVIEW software (Version 2011 SP1, National Instruments Corp., Austin, TX).
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The PROSE model was especially designed to simulate the impact on the river of both permanent dry-weather effluents and of highly transient Combined Sewer Overflow (CSO).
As expected, the model results predict a reduction of both permanent dry-weather effluents and CSOs in the future that will greatly improve the oxygen levels (concentrations higher than 7.3 mgO2 L− 1, 90% of the time instead of 4.0 mgO2 L− 1 in the late 90s).
There was no significant deactivation of the catalyst over 1000 h of continuous operation and the CO concentration in the reformate effluent dry gas was less than 1.4%, and methane produced was negligible under the molar ratios of O2/MeOH = 0.3, H2O/MeOH = 1.2, and gas hourly space velocity equal to 3850 h−1.
After precipitation, the samples were washed with deionized water up to pH 7 of the effluent; dried under vacuum conditions at 343 K down to constant mass, treated with ultrasound at 30 kHz using Bandelin ultrasonic bath (Bandelin, Hungary), and dried in a desiccator over CaCl2 at 293 K.
During the wet season agricultural runoff and combined sewer overflows (CSO) were responsible for nutrient discharges, while during the dry season partially treated effluent from wastewater was the main nutrient source.
Another part of the regeneration is provided either by a dry cooler or an effluent stream from the municipal wastewater treatment plant (MTP).
The small makeshift hanging latrines built by the community during the dry season discharge their effluent directly into the waters below, polluting the environment in which people live and work.
The Nishitakase carries mostly STP A and STP B effluent on dry days, resulting in its high concentration.
The FSTP consists of settling/thickening tanks followed by unplanted drying beds, with the effluent going to the WWTP.
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