A process for controlling the aeration rate during the aerobic phase of a wastewater treatment process is disclosed, which comprises: (a) measuring at moment t.sub.1 the ammonium concentration [NH.sub.4.sup.+].sub.1 and nitrogen oxide concentration [NO.sub.x].sub.1 in a mixture of wastewater and microbial sludge; (b) determining a nitrogen oxide target concentration [NO.sub.x].sup.F.sub.1 at the end of the aerobic phase based on at least the current ammonium concentration [NH.sub.4.sup.+].sub.1 and the current NO.sub.x concentration [NO.sub.x].sub.1; (c) determining a setpoint [NO.sub.x].sup.SP.sub.1 based on interpolation between [NO.sub.x].sub.1 and [NO.sub.x].sup.F.sub.1; (d) adjusting the aeration rate to minimise error between [NO.sub.x].sub.1 and [NO.sub.x].sup.SP.sub.1; and (e) repeating steps (a) to (d) at further moments t.sub.1. The invention further concerns a process for the treatment of wastewater, using the process.

A water treatment system, a water treatment monitoring and/or control system, and a method of monitoring and/or controlling treatment of water are disclosed. The water treatment system generally includes a water pump configured to supply water from a water source to an intake pipe, a chlorine source pump configured to supply a chlorine source from a storage vessel to a chlorine source feed line, a water flow and/or pressure switch configured to detect a positive water flow and/or pressure in the intake pipe, a chlorine flow monitor, and logic or circuitry configured to notify a user and optionally automatically disable or turn off the water pump when (1) the water flow and/or pressure switch detects the positive water flow and/or pressure in the intake pipe and (2) the chlorine source flow monitor detects either that (i) the chlorine source pump is not primed or (ii) there is no flow in the chlorine source feed line. The chlorine flow monitor is configured to determine (a) whether the chlorine source pump is primed or (ii) there is no flow of the chlorine source in the chlorine source feed line. The monitoring/control system and method generally embody one or more of the inventive concepts disclosed herein.

An ultrapure water manufacturing facility includes: a supply line connected to a pure water storage tank and in which a plurality of pure water treatment devices are sequentially arranged; a branch line branched downstream of the supply line and connected to the pure water storage tank; and a first automatic valve connected to the branch line and configured to be actuated by a double-acting actuator.

A space habitat includes a water processing assembly including a wastewater tank and a water processing section connected to the wastewater tank. The water processing section includes a pump to urge flow of the wastewater, a mostly liquid separator to separate gas from liquid in the wastewater, a catalytic reactor located downstream of the mostly liquid separator, and one or more sensors located downstream of the catalytic reactor to determine if the wastewater is sufficiently processed. A valve directs the wastewater to a water storage tank if the sensors determine that the wastewater is sufficiently processed, and direct the wastewater to the wastewater tank if the one or more sensors determine that the wastewater is not sufficiently processed. The space habitat further includes one or more of a carbon dioxide removal system, a trace contaminant removal system, a temperature and humidity control system or a waste collection system.

Fluid purification systems employing a monolithic composite photocatalyst to remove volatile organic compounds (VOCs) and/or pathogenic organisms are disclosed. Pairing of systems tuned to abate each of these materials are discussed in different configurations such as series and parallel, as well as combining systems to target both materials simultaneously. System configurations that allow a portion of the fluid stream to be purified are also disclosed as are configurations that allow regeneration of the photocatalyst. These features may be augmented by sensors that allow closed loop control of bypass and regeneration cycles in the systems.

A dynamic multi-objective particle swarm optimization based optimal control method is provided to realize the control of dissolved oxygen (S.sub.O) and the nitrate nitrogen (S.sub.NO) in wastewater treatment process. In this method, dynamic multi-objective particle swarm optimization was used to optimize the operation objectives of WWTP, and the optimal solutions of S.sub.O and S.sub.NO can be calculated. Then PID controller was introduced to trace the dynamic optimal solutions of S.sub.O and S.sub.NO. The results demonstrated that the proposed optimal control strategy can address the dynamic optimal control problem, and guarantee the efficient and stable operation. In addition, this proposed optimal control method in this present invention can guarantee the effluent qualities and reduce the energy consumption.

The present invention relates to a method of evaluating and optionally selecting a suitable chemistry for removal of microplastics in a liquid matrix, said method comprising using at least one coagulant and/or flocculant and measuring fluorescence intensity and light scattering intensity of any particles in a sample volume of clarified liquid matrix by an optical measurement.

An autonomous and independent biofouling detecting system for detecting biofouling associated with a plant membrane based on a test membrane. The biofouling detecting system includes the test membrane, which shares a feed with the plant membrane; a molecule detecting sensor that detects a presence of a molecule associated with biofouling of the test membrane; and a global controller that controls a flow of the feed through the test membrane and determines when the test membrane needs cleaning.

A method and system for reducing ion concentration of a solution and converting gas. The system comprising a multi-chamber unitary dialysis cell comprising a gas chamber, a product chamber, and an acid chamber. Ion exchange barriers separate the chambers of the dialysis cell. A first anion exchange barrier is positioned between the product chamber and the acid chamber and a first cation exchange barrier is positioned between the product chamber and the gas chamber. Anions from the solution being treated associate with cations from the acid chamber to form an acid solution in the acid chamber, and cations from the solution being treated associate with anions from the fluid comprising gas to form salt, thereby reducing the ion concentration of the solution being treated and converting at least a portion of the gas into salt.

A transportable modular system for emergency treatment of water polluted by liquid hydrocarbon spillage comprises: at least a first containerized treatment module, comprising a container in the form of a standard size intermodal container which houses a coalescence separator device, configured to operate an oil/water separation; a suction pipe having a first end connected to the coalescence separator device and a second end provided with an inlet connected to at least one floating skimmer; a pump positioned on the suction pipe; a water drain pipe and an oil drain pipe, connected to a water outlet and an oil outlet, respectively, of the coalescence separator device.