Treatment chemicals (for example, scale inhibition chemicals) can be applied to fluids in a pipeline by diverting a side stream of the produced water from a pipeline into a vessel containing a solid material to release of an active fluid treatment agent from the solid material into the diverted produced water; merging the diverted produced fluid containing the active fluid treatment agent into the pipeline; and adjusting a flow rate of the diverted side stream of the produced water to change a level of the active fluid treatment agent in the flow of produced water in the pipeline. Treatment systems can include a pipeline, a vessel containing a solid treatment material; a bypass line providing a fluid connection between the pipeline and an inlet of the vessel; and a return line providing a fluid connection between an outlet of the vessel and the pipeline.

A water treatment system and a ballast water treatment method. A ballast water treatment system according to an embodiment of the present invention comprises: a first ballast water supply pipe for receiving a supply of ballast water from a first sea chest positioned in a non-explosion-proof area of a ship; an electrolytic bath for electrolyzing the ballast water supplied from the first ballast water supply pipe; a second ballast water supply pipe for receiving a supply of ballast water from a second sea chest, which is positioned in an explosion-proof area of the ship, and supplying the ballast water to a ballast tank of the ship; a filter provided to the second ballast water supply pipe so as to filter the ballast water passing through the second ballast water supply pipe; and a third ballast water supply pipe connected to the second ballast water supply pipe so as to supply the ballast water, which has been electrolyzed from the electrolytic bath, to the ballast water which has passed through the filter.

A biological reactor system treats concentrated contaminated water with a combination of upflow and downflow bioreactors that are downstream from a reverse osmosis or other concentrator. The system may have a fail safe configuration where flush water may be introduced to the reactors in the event of a power failure or when taking the reactors offline. Many reverse osmosis systems introduce antiscalant treatments upstream so that the reverse osmosis filters do not scale. However, such treatments result in superconcentrated conditions of the antiscalants in the contaminated water processed by the bioreactors. A flushing system may deconcentrate the bioreactors to prevent the antiscalants from precipitating and fouling the bioreactors.

Disclosed is a filter assembly capable of adjusting elimination of solid materials using a flow-variable bypass flow path. The filter assembly includes a filter portion (100) which includes a cover portion (110) formed on top to have a shape in which a bypass flow pipe (112) and a water discharge pipe (113) sequentially surrounds a perimeter of a vertically protruding original water inflow pipe (111) in a stepped structure and accommodates a filter body therein and a filter cartridge header (200) in which the cover portion (110) of the filter portion (100) is accommodated therebelow and which includes a bypass flow rate control unit (300) capable of adjusting an inflow amount of original water flowing into the bypass flow pipe (112).

The present invention relates to a method for the treatment of organic matter, in particular sewage sludge, where the organic matter is first fed to a disintegration system. The organic matter is then subjected to thermal hydrolysis in the disintegration system to form disintegrated matter. The disintegrated matter is fed to a digester in which the disintegrated matter is at least partially digested such that digested sludge is formed, where at least part of the digested sludge obtained is recirculated via a recirculation line to a point upstream of the disintegration system. The invention further relates to a device for the treatment of organic matter, in particular sewage sludge, comprising a disintegration system, a digester downstream thereof, and a recirculation line for at least partially digested disintegrated matter, said recirculation line extending from a point downstream of the digester to a point upstream of the thermal disintegration system.

Provided are a water treatment apparatus and a water treatment method capable of performing a significant water quality evaluation of treated water before the filtration process, and capable of rapidly responding to a change in water quality of the treated water. A water treatment apparatus of the present invention includes a treated water filtering unit which filters treated water supplied from a treated water line to become filtered water, a filtered water mixing unit which is provided in a treated water extraction line diverging from the treated water line to reduce a turbidity concentration in the treated water of the treated water extraction line to become measured water, and a water quality measuring unit which is provided at a rear stage of the filtered water mixing unit in the treated water extraction line and measures water quality of the measured water to evaluate the water quality of the treated water.

Embodiments of the present invention are directed to water treatment systems and methods offering improved efficiency, longevity and versatility. More specifically, water treatment systems and methods configured in accordance with the present invention provide for dynamic bypass of one or more water treatment stages by at least a portion of water being treated. Dynamic bypass reduces the amount of work expended by water treatment system components to treat a given volume of water. Thus, by adjusting such work expended based on a target water quality, the water treatment system can conserve power, extend system up-time, reduce usage of system consumables, potentially remediate a fault in a treatment stage under certain conditions, avoid the need for designing different systems for different conditions, and support automation of system operation.

An apparatus for filtering water has an interface and a filtration/purification canister removably mountable thereon. Connecting the canister to the interface automatically opens a check valve in the interface to permit water to flow from the interface into and through the canister, and then back to and through the interface to an outlet port. Disconnecting the canister from the interface automatically closes the check valve, stopping the flow of water. An end cap may be substituted for the canister to permit fluid to flow through the interface when the canister is not mounted on the interface. The outlet port may be directly connected to an appliance that uses water, to eliminate possible contamination that may occur when water is brought indirectly form the outlet port to the appliance instead. A flapper valve is provided in the canister to prevent back flow of fluid from the inlet port of the canister when the canister is not mounted on the interface. The flapper valve also is provided with an actuating means to automatically open the flapper valve when the canister is mounted on the interface, which permits fluid to be drained from the canister when the fluid distribution system is being drained without disconnecting the canister from the interface.

A filter cartridge (5) with a housing enclosing a filter volume filled to about 80% with a filter granulate (15) is screwed into a joint (7) of a connecting piece (1) by means of a port (12) ending in an outflow opening (13) and being connected to an outlet line formed by a second fitting (3), and surrounded with a distance by a casing (4) that is screwed to the connecting piece (1). An inlet line formed by a first fitting (2) opens into an intermediate volume (6) lying between the casing (4) and the outer side of the filter cartridge (5) in such a way that untreated water enters into the outlet line via the intermediate volume (6) and through the bottom (9) which is perforated by slots (10), the filter granulate (15), the intermediate floor (11) that is likewise slotted and the port (12). In order to reduce the flow resistance, the port (12) is provided with bypass openings (14) to allow untreated water to pass also directly out of the intermediate volume (6) into the port (12).

An apparatus, system, and method for sanitizing water contained in a pool or a tank, includes a container to hold zeolite crystals that provide a benefit, in a first mode of operation, of removing urea and ammonia from the water as the water passes through the container and the held zeolite crystals, the held zeolite crystals removing the urea and ammonia from the water by retaining the urea and ammonia as the water passes through the container and held zeolite crystals. A switching mechanism permits the held zeolite crystals to undergo a switch into a second mode of operation during which the held zeolite crystals are exposed to a brine solution that reconditions the held zeolite crystals by desorbing from the held zeolite crystals the urea and ammonia that had been adsorbed by the held zeolite crystals during the first mode of operation.