Coking effluent carries roughly 500 identified compounds, surplus nitrogen and a BOD5/COD ratio near 0.3, which caps what biology can do on its own. This piece walks the numbers that decide the flowsheet, why plain activated sludge stalled, how advanced o
Ultrafiltration sits between microfiltration and reverse osmosis, and selecting a membrane means choosing a pore size, a material and a cleaning regime together. This article covers PVDF and PES against PAN, PVC and ceramic alternatives, the construction
Ammonia nitrogen can be measured by Nessler colourimetry, the salicylate-hypochlorite method, an ammonia gas-sensing electrode, or distillation followed by titration. This article sets out the detection limits, working wavelengths and interference profile
Stabilization ponds treat wastewater and produce biomass at the same time, which makes them a resource unit as much as a treatment step. This guide sets out how anaerobic, facultative, aerobic and aerated ponds differ, the loading and geometry parameters
Total phosphorus is measured only after digestion converts every form in the sample to orthophosphate, and most of the error lives in that step. This article covers the national standard ammonium molybdate methods, the digestion options and their practica
Biological contact oxidation borrows from both biofilm and activated sludge practice, and most of its behaviour comes down to filler selection. This guide covers how pore size is matched to BOD5 and suspended solids, what three-dimensional elastic filler
A UASB reactor lives or dies on granular sludge and on the three-phase separator that keeps it inside the vessel. This article works through the reactor internal zones, the biomass concentrations and settling behaviour that define a healthy bed, the three
Anaerobic treatment is often introduced as a sludge and energy story, but what decides whether a digester holds is the sequence of hydrolysis, acidification, acetogenesis and methanogenesis running in balance. This piece walks through all four stages with
Battery-material lines set tight purity limits on nickel sulfate, ammonium sulfide and sodium sulfate product liquids, and emulsified oil is the contaminant that keeps shifting the goalposts. This article follows the CDOF integrated ozone catalytic oxidat
Two configurations cover most desalter wastewater duties: a coalescing oil remover followed by CDFU cyclonic dissolved air flotation, or two CDFU stages in series. Both deliver effluent under 50mg/L and above 90% removal with no chemical dosing. This guid