Early detection, at the outlet of the WWTP, of the risk of non-compliance with the legal levels required in the authorization. This detection allows the addition of inhibitors or reagents (e.g. defoamers) for immediate management, improving plant efficiency and optimizing additive costs

Early detection of unexpected spills at the inlet of both urban/assimilable and industrial treatment plants. This detection allows both detour or diversion of the discharge to containment tanks for further treatment, and the addition of inhibitors or reagents for immediate management (such as ferric chloride, urea or phosphoric acid to increase or decrease phosphorus and total nitrogen levels). This helps to improve the efficiency and effectiveness of the wastewater treatment process prior to reuse and delivery to the natural environment

Continuous monitoring of basin points with high discharge pressure or located in places with high environmental risk: waters below metropolitan areas, industrial estates, airports and logistic centers or areas with high diffuse pollution from intensive agricultural areas

Continuous monitoring of freshwater catchment and potabilization/desalination processes to allow early detection of problems related to turbidity, algae blooms and uncontrolled discharges (such as grease and oils)

Continuous individualized control of the discharge point (point of contact between the effluent and the receiving environment). Helps to ensure regulatory compliance with the legal levels required in the authorization

Continuous control of homogenization ponds and tanks for the addition of inhibitors or reagents, such as caustic soda or sulfuric acid to increase or decrease the pH levels of the homogenized water. This helps to improve plant efficiency

Continuous control of desanding and degreasing processes for the addition of inhibitors or reagents, such as coagulants or flocculants, prior to primary settling. This helps to improve plant efficiency and cost savings in reagents

Continuous control of biological reactors for oxygenation control and management of blowers and aerators, prior to secondary settling. This helps to improve plant efficiency by saving energy consumption costs and guaranteeing the quality of the bacterial liquid

Continuous monitoring of the outlet water after clarification processes for the addition of oxidants and disinfectants, such as ozone or defoamers, prior to leaving the plant. This helps to improve plant efficiency by saving costs and effectiveness while complying with regulatory standards

Continuous control of the evolution of any spillway point, both from the quantitative point of view of quantity of spillway and from the qualitative point of view of load or quality of the spillwayed. This helps to have a continuous data of when and how much is happening at that spillway point

Continuous monitoring of the centrifuge return evolution, both from the quantitative point of view of return quantity and from the qualitative point of view of centrifuge load or quality. This helps to have a continuous data of how the return can affect the inlet and therefore the rest of the purification processes; being able to divert for individual treatment or recirculate water from the inlet to minimize the inlet load

Continuous control of the drainage of filtration or centrifugation systems in sludge dewatering processes, for the addition of reagents, such as polyelectrolytes. This helps to reduce the sludge volume to a minimum and thus improve plant efficiency and save costs

Continuous monitoring of drinking water distribution tanks and reservoirs to allow early detection of turbidity and color problems

Continuous control of the situation of a stormwater detention vault, both from the quantitative point of view of quantity and from the qualitative point of view of tank quality. This helps to have a continuous data of when and how much is happening in that tank and to be able to discharge or divert to treatment