A solids separation apparatus (SSA) for removing solids concentrate from a continuous fluid stream. The solids separation apparatus includes a tower. The SSA includes a transducer operably engaged with a first end of the tower and configured to generate a standing sonic wave inside of the tower. The SSA also includes a reflector operably engaged with an opposing second of the tower and configured to reflect the standing sonic wave towards the transducer. The SSA also includes at least one set of ports defined in an interior wall of at least one solids removal stage of the tower. The at least one set of ports is positioned at anti-nodes of the standing sonic wave to recover solids concentrate from a fluid stream flowing through the tower. The transducer and the reflector of the SSA are linearly moveable relative to the tower to linearly move the standing sonic wave.

The present disclosure relates a system for the treatment of water. The water treatment system may be linked an aquatic protection system or a water filtration system.

The invention provides an irradiation device (1) designed to be mounted to an irradiation reactor (20), comprising: an irradiation source (2), preferably an UV-LED, mounted on a heat conductive substrate (3); a disk-like heat sink (4) configured to removably receive the conductive substrate (3) such that heat transfer from the substrate (3) to the heat sink (4) is possible at a contact surface (4a) and such that the irradiation from the irradiation source (2) can pass through an opening (5) of the heat sink (4) into aninterior volume (21) of the irradiation reactor (20) when the irradiation device (1) is mounted to the irradiation reactor (20), wherein the opening (5) of the heat sink (4) is closed by a quartz window (6); fixation means (7) releasably biasing the substrate (3) against the contact surface (4a) of the heat sink (4); and a fluid channel (8) extending along and/or through the heat sink (4), wherein the fluid channel (8) is arranged to communicate with a fluid inlet or outlet port (22) of the irradiation reactor (20) and with one or more outlet openings (9) for discharging the fluid into the interior volume (21) of the irradiation reactor (20) or with one ore more inlet openings (9) for feeding the fluid from the interior volume (21) of the irradiation reactor (20) into the fluid channel (8).

The present invention discloses a treatment process for a submerged lifting circulation type bio-membrane filter, wherein the treatment process comprises the following steps: two groups of symmetrically staggered filter curtains (2A and 2B) are adopted; the two groups of filter curtains (2A and 2B) are periodically lifted up and down in a reciprocating manner in a biofilter (1) under the action of a lifting mechanism (4), so that bio-membranes on the two groups of filter curtains (2A and 2B) are in contact with the atmosphere and sewage in turns, absorb organic matters in the sewage when lifting down for submerging, absorb oxygen when lifting up and exposing into to the atmosphere, and bring oxygen into the sewage and cause sewage turbulence in a water tank when lifting down for submerging again, so that the dissolved oxygen is uniformly distributed, thereby purifying the sewage.

Metal working fluid decontamination apparatus (10) includes: an intake arrangement (40) for metal working fluid (42); a pump (16) for providing, in use, flow pressure to the metal working fluid (42); a decontaminator (50) for reducing contamination in the metal working fluid (42); and an outlet arrangement (34) for the metal working fluid. The metal working fluid (42) is a fully synthetic metal working fluid, which comprises water and a water soluble synthetic concentrate which does not comprise oil.

Embodiments of the present invention provide the integration of arbitrary flow directing patterns, deposited or integrated on or into the porous permeate spacer in a spiral-wound membrane separation element.

A method of decomposing a fluidic product (110) having a plurality of particles (112) is disclosed. The method includes inductively heating the fluidic product (110) at a first predetermined temperature while flowing through a temperature rising portion (138) having a first heating region formed of at least one metal pipe (124) by using a first heating induction coil (134) surrounding the first heating region; holding a temperature of the fluidic product (110) at approximately the first predetermined temperature for a predetermined reaction period while flowing through a temperature holding portion (140) having a second heating region formed of at least one metal pipe (124) by inductively heating the temperature holding portion (140) using a second heating induction coil (136) surrounding the second heating region; and decomposing the fluidic product (110) while flowing through the temperature rising portion (138) and the temperature holding portion (140) during the predetermined reaction period.

A hydrothermal liquefaction (HTL) system can comprise a biomass slurry source, a first pump in fluid communication with the slurry source and configured to pressurize a biomass slurry stream from the slurry source to a first pressure, a first heat exchanger in fluid communication with the first pump and configured to heat a slurry stream received from the first pump to a first temperature, a second pump in fluid communication with the first heat exchanger and configured to pressurize a slurry stream received from the first heat exchanger to a second pressure higher than the first pressure, a second heat exchanger in fluid communication with the second pump and configured to heat a slurry stream received from the second pump to a second temperature higher than the first temperature, and a HTL reactor configured to produce biocrude from a slurry stream received from the second heat exchanger.

A system and method for evaporative treatment or wastewater which minimizes scaling and system maintenance is disclosed. The apparatus can include an evaporation vessel with a heating source to evaporate water from a solution under treatment and a drain valve for draining the solution after treatment. The apparatus can also include one or more sensors configured to measure parameters of a solution under treatment and a user programmable controller to control the treatment process based on such measurements. A user can configure the controller to define the detection of a solution's critical state where contaminant concentrations are maximized yet scaling is minimized. When a critical state of the solution is reached a portion of the treated solution can be removed and the vessel refill with new wastewater thereby lowering the concentration of the remaining solution the repealing the evaporation and drain cycle until all wastewater has been treated.

A water processing system is provided for processing or conditioning water to be distributed to a downstream function or system. The system includes a water processor with a conditioning element disposed inside a housing between an inlet and outlet of the housing. The conditioning element includes a series of plates having apertures with sharp edges to direct the flow of water and facilitate splitting of small gas bubbles into even smaller nano-bubbles. The plates may have different configurations of apertures. Optionally, a mixer injector introduces a gas, in the form of gas bubbles, into the water flow upstream of the water processor. The injector introduces additional gas volume in the form of relatively large bubbles, which are subsequently split into smaller bubbles (including nano-bubbles) in the water processor.