Abstract:
Catalytic water treatment is provided using an active material driven with an optical and/or electrical excitation. The active material is MoS2, MoSe2, WS2, WSe2, MoxW1−xS2, MoxW1−xSe2, MoSySe2−y, WSySe2−y, or MoxW1−xSySe2−y; wherein 0
Abstract:
Purifying apparatus, and related purifying method, comprising a reactor (40) and one or more light sources (210), wherein the reactor (40) is configured to receive a light irradiation emitted by said one or more light sources (210) a nd to contain inside a fluid (50) to be purified and at least one catalyst configured to absorb said light irradiation and to activate at least one photocatalysis that removes at least one polluting substance inside the fluid (50), wherein the purifying apparatus comprises switching means (240) configured to be supplied by at least one power supply apparatus (10, 30, 220) a nd to drive said one or more light sources (210) in dimming mode according to a dimming duty-cycle t ON / T dim , wherein said one or more light sources (210) are kept on for a switching-on time tow within a dimming period T dim , where t ON ≤ T dim , and kept off for a switching-off time t OFF , equal to (t dim - T ON ), wherein the purifying apparatus comprises processing and control means (230, 250, 270) configured to send to said switching means (240) a dimming signal d LED (t), that is time-varying, equal to the instantaneous dimming duty-cycle t ON /T dim according to which said switching means (240) drives said one or more light sources (210) in dimming mode, the purifying apparatus being characterised in that the dimming signal d LED (t) that said processing and control means (230, 250, 270) is configured to send to said switching means (240) has a waveform selected from or equal to a combination of waveforms selected from the group comprising or consisting of: - periodic waveforms, - pseudo-periodic waveforms.
Abstract:
The invention relates to a multi-stage distillation system (1) having stages Si, where i=1,...n, wherein during operation, each stage Si works in a higher pressure and temperature range (Pi, Ti) than the following stages Si+1, wherein each stage Si comprises an evaporator Ei and a condenser Ci, wherein each evaporator Ei and each condenser Ci comprises a pressure-tight container (2) having a steam chamber (6), wherein the steam chamber (6) of each evaporator Ei is in pressure-connection with the steam chamber (6) of the condenser Ei of the same stage Si via a steam pipe (7) having a large cross-section. Each outlet (5) of each evaporator Ei is connected to a spray inlet (3) of the next evaporator Ei+1, and the outlet (5) of the last evaporator En is connected to the spray inlet (3) of the first evaporator E1 with a respective fluid line (8) to form an evaporator circuit, and each outlet (5) of each condenser Ci is connected to the one pray inlet (3) of the previous condenser Ci-1, and the outlet (5) of the first condenser C1 is connected to the spray inlet of the last condenser Cn with a fluid line (9) to form a condenser circuit. According to the invention, at least one steam line (10) is connected by a first end to one of the fluid lines (9) between condensers Ci+1 and Ci or to the fluid line (8) between the evaporators En and E1, and is connected by a second end to a steam chamber, which, during operation, has a higher pressure P than the pressure Pi in the steam chamber (6) of the condenser Ci or than the pressure P1 in the steam chamber (6) of the evaporator E1. The invention also relates to a method for carrying out a distillation in a system according to the invention, as well as a controller.
Abstract:
Provided are a desalination plant mounted on a barge and a method for placing the same. The barge is constructed to float on the sea, and the desalination plant is constructed to draw seawater from the sea and desalinate the seawater into freshwater. The desalination plant mounted on the barge is placed on a heavy lift vessel, tugged by a tugboat, and installed in the seashore of a water-scarcity area or island area.
Abstract:
Systems, apparatuses, and methods of treating wastewater are provided. In some aspects, a container may be provided and may include a first member, a second member spaced apart from the first member, and media supported by and extending between the first and second members. An organism may be introduced into the container and wastewater may be introduced into the container for treatment. The media may be loop cord media. In other aspects, two containers may be provided and wastewater may be initially introduced into a first container for treatment, removed from the first container, and subsequently introduced into the second container for further treatment. A first species of organism may be present in the first container and a second species of organism may be present in the second container. Methods of using these containers are also provided.
Abstract:
The present invention relates to a flow device for "anti-legionnaires' disease" sanitization of branch lines and terminal apparatuses of water systems, comprising a control unit (3), provided with memory and microprocessor with a sanitization cycle program, as well as an electrovalve (1) connected to said control unit (3) and a by-pass pipe (7, 8, 9) along which said electrovalve (1) is mounted.
Abstract:
A liquid container (400) for containing a liquid is proposed. The liquid container (400) comprises a seat (148) for housing a liquid filtering unit (139) adapted to filter said liquid, a flowing section (148), through which said liquid is made to flow, and a sensing arrangement comprising at least one probe element (457) responsive to the presence of liquid and coupled or couplable with a data processing element (442). The liquid container further comprises a liquid flow-regulating element (139; 460) associated with the flowing section (148) and adapted to impose a predetermined flow rate ( ff, ff', fr) to a flow of liquid flowing through the flowing section (148) and wherein the sensing arrangement is configured to measure a time interval (ti, t' j , t" k ) during which the liquid flows through the flowing section (148) at said predetermined flow rate, the data processing element (442) being configured to calculate a volume (Vol i , Vol' j , Vol" k ) of liquid flowed through the flowing section (148) based on the measured time interval (ti, t' j , t" k ) and the predetermined flow rate (ff, ff', fr), said volume of flowed liquid being related to the volume of liquid filtered by said liquid filtering unit.
Abstract:
A method comprising the steps of flowing a flow of relatively cold fluid along at least one photovoltaic solar panel being heated by solar energy towards and into a fluid treatment device, at least heating the flow of fluid in a fluid treatment device to divide the flow of fluid into a flow of a first fluid part and a flow of a second fluid part, flowing the flows of the first fluid part and the second fluid part from the fluid treatment device along the flow of relatively cold fluid. Before entering the fluid treatment device the flow of relatively cold fluid is preheated by the relatively warm photovoltaic solar panel and the relatively warm flow of the first fluid part and the relatively warm flow of the second fluid part.
Abstract:
The present invention refers to a process for the preparation of an aqueous solution comprising at least one earth alkali hydrogen carbonate and its uses. The process is carried out in a reactor system that comprises a tank (1) equipped with a stirrer (2) and at least one filtering device (4).
Abstract:
Described herein are a method and system for desalinating saltwater using concentration difference energy. A “five stream” dialytic stack is described that can be used to desalinate saltwater at a relatively high recovery ratio. The dialytic stack may include, for example, one or more drive cells having a paired concentrate and a diluent-c chamber in ionic communication with a product chamber that is adjacent to an anion and a cation discharge chamber each filled with diluent-p. The drive cell applies a drive voltage across the product chamber, and when the drive voltage exceeds a desalination voltage of the product chamber, the saltwater in the product chamber is desalinated. The diluent-p may be at a lower ionic concentration than the diluent-c, which may be at a lower concentration than the concentrate. The relatively high concentrations of the concentrate and the diluent-c facilitate a relatively high recovery ratio, while the relatively low concentration of the diluent-p facilitates a relatively low desalination voltage. The dialytic stack may accept brine discharged from a first desalination plant and may use this brine as a source of the concentrate, diluent-c, or diluent-p. Alternatively, the dialytic stack may accept the brine as saltwater to be desalinated, and may then output desalinated brine back to the first desalination plant for further desalination. Processing the brine in the dialytic stack may decrease its volume, decreasing costs associated with treating or otherwise disposing of the brine.