Abstract: A computerized process for controlling an air purification system comprises a bioreactor in particular, the system may include a photobioreactor for treating urban air, in particular for CO2 removal. The system may be connected to the sanitation network and/or to a (drinking and/or municipal) water supply network. The connection and the drainage system may in particular maintain a fluidic isolation between the two types of networks. The system may optionally be equipped with measurement sensors and/or actuators that make it possible to control the internal activity of the bioreactor. Various control modes of a grid of bioreactors are described. Data on the status of the connected networks (e.g. water, sanitation, cooling, heating networks) contribute to the control of a network of geolocalized bioreactors. The software aspects are described. The supervision of the grid of bioreactors may in particular be carried out remotely via onboard communication devices.

Abstract: A computerized process for controlling an air purification system comprises a bioreactor in particular, the system may comprise a photobioreactor for treating urban air, in particular for CO2 removal. The system may be connected to the sanitation network and/or to a (drinking and/or municipal) water supply network. The connection and the drainage system may in particular maintain a fluidic isolation between the two types of networks. The system may optionally be equipped with measurement sensors and/or actuators that make it possible to control the internal activity of the bioreactor. Various control modes of a grid of bioreactors are described. Data on the status of the connected networks (e.g. water, sanitation, cooling, heating networks) contribute to the control of a network of geolocalized bioreactors. The software aspects are described. The supervision of the grid of bioreactors may in particular be carried out remotely via onboard communication devices.

Abstract: Device for treating waste water, especially rainwater by jointly carrying out degritting, degreasing and settling, which includes a degritter fitted with a grit trough, passed through by a descending then ascending flow of the water to be treated, a degreasing surface provided above a part of the degritter and the feed region of the settling tank, and a settling tank which includes a feed or presettling basin, a floor, a laminar settling region and an extraction trough, wherein the partition separating the degritter from the settling tank includes a flap valve making it possible, when it is open, to transfer the untreated water without perturbation towards the settling tank, and therefore allowing correct settling during this filling phase.

Abstract: A system for treating organic emulsions by separating by coalescence the disperse phase from the dispersion phase of the emulsion includes a single enclosed chamber having therein a lower destabilizing area, a central filtering and coalescence area, and an upper flotation and separation area. An emulsion to be treated is continuously introduced and passed upwardly through the destabilizing area, the filtering and coalescence area and the flotation and separation area. The flotation and separation area includes a center portion positioned vertically above the filtering and coalescence area and at least one lateral portion in flow communication with the center portion and extending laterally downwardly along a side of the filtering and coalescence area and the destabilizing area. The lateral portion of the flotation and separation area is laterally separated from the filtering and coalescence area and from the destabilizing area by a partition.

Abstract: A single enclosed chamber includes a lower destabilizing area, a central filtering and coalescence area containing coalescence material, and an upper flotation and separation area. Emulsion is introduced into the lower destabilizing area and is destabilized therein. The emulsion is then passed upwardly into the central filtering and coalescence area. The dispersed phase of the emulsion is attracted to the coalescence material in the form of droplets, and as the emulsion continues to pass upwardly therethrough the droplets grow in size. During passage of the emulsion through the filtering and coalescence material, matter in suspension is filtered from the emulsion. Within the flotation and separation area is located a separation device including a lower convergent portion and an upper divergent portion.