A device and a method for detecting deposits in a membrane module which produces a permeate and which comprises at least one permeable or semipermeable membrane layer. At least one polymer optical fiber for detecting deposits on the membrane layer is integrated in the membrane module such that the polymer optical fiber is in contact with at least one membrane layer. A method of detecting deposits in a membrane module producing a permeate and to a membrane module for producing a permeate from a feed stream of a fluid, in particular an aqueous solution, with the membrane module comprising a plurality of adjacently disposed or stacked sheets of a permeable or semipermeable membrane layer and with at least one polymer optical fiber being embedded or integrated in the membrane module, which polymer optical fiber is in contact with at least one sheet of the membrane layer.

A filter device includes an inlet manifold, an outlet manifold and membrane filter units. Each membrane filter unit has an inlet opening for a fluid flow to be processed, a first outlet opening for a retentate portion of the fluid flow, and a second outlet opening for a remaining portion of the fluid flow. Each inlet opening is fluidly connected to the inlet manifold, and each first outlet opening is fluidly connected to the outlet manifold. The two membrane filter units are staggered and are not axially aligned with respect to each other. One of the membrane filter units is fluidly connected to the inlet manifold and to the outlet manifold via a first set of conduits, and the other membrane filter unit is fluidly connected to the inlet manifold and to the outlet manifold via a second set of conduits.

A membrane filter configured to filter a liquid, the membrane filter including a base element including at least one membrane carrier that is externally flowable by the liquid and a gas; hollow fiber membranes respectively including lumen and attached at a top of the at least one membrane carrier wherein a liquid permeate is filterable from the liquid into the lumen; a one piece extruded circumferentially closed pipe that envelops the hollow fiber membranes; a gas inlet configured to let gas into a bottom of the membrane filter; at least one permeate collection cavity included in the base element and connected with the lumen and configured to collect the liquid permeate from the hollow fiber membranes; a permeate outlet included in the base element and configured to drain the liquid permeate from the at least one permeate collection cavity laterally from the base element.

A separation device includes a membrane separation module (10), an adsorption module (20), and a gas intake module (30). The membrane separation module includes a first housing (110), and a membrane assembly (130) disposed in the first housing. The first housing has a first gas inlet (121), a first gas outlet (122), and a retentate gas outlet (123). The membrane module has a permeate gas outlet, the permeate gas outlet being in communication with the first gas outlet. The adsorption module has a second housing (210) and an adsorbent layer (230) disposed in it. The second housing is disposed on the first housing and has a second gas inlet (221), a second gas outlet (222), and a desorption gas outlet (223). The second gas inlet is in communication with the first gas outlet. The gas intake module has a third gas outlet (321) in communication with the first gas inlet.

A separation membrane module that is provided enables a bending load that is applied to a support member that supports ends of tubular separation membranes to be decreased and enables a seal member between the outer circumferential surface of the support member and the inner circumferential surface of a housing to be omitted. The separation membrane module includes a tubular housing 2, tubular separation membranes 3 that are arranged in a longitudinal direction of the housing 2, end tubes 4 that are connected to the lower ends of the tubular separation membranes 3, a support box 5 that supports the end tubes 4, and a backpressure chamber 16 below the support box 5. The tubular separation membranes 3 are in communication with a collection chamber 5v of the support box 5. A permeated fluid is extracted via a nozzle 5n that is disposed on the support box 5. A chamber 11 and the backpressure chamber 16 are in communication with each other via a gap between the outer circumferential surface of the support box 5 and the inner circumferential surface of the housing 2. Pressure in the chamber 11 and pressure in the chamber 16 are substantially the same.

Filter arrangements comprising a plurality of radially arranged filters, each filter comprising a plurality of arms, each arm comprising a hollow tube having porous side wall, each hollow tube having an open first end and an open second end, and a tube inner fluid channel having an inner diameter; the filter further including a first tube connector, comprising a first hollow body having porous side walls and a first hollow body inner diameter, connected to, and in fluid communication with, the hollow tubes, and a second tube connector, comprising a second hollow body having a second hollow body inner diameter, connected to, and in fluid communication with, the first hollow body, and filter devices including filter arrangements, and methods of use are disclosed.

The invention relates to a modular flow system having a plurality of frame elements (101, 102) configured to be combined together to form a stack for forming a functional member such as in particular a membrane distillation stage, a vapor generator, a condenser, a heat exchanger, a filter and/or a pervaporation stage, wherein the frame elements (101, 102) each include: an outer frame (39) and an inner frame (43), the inner frame (43) encasing a central inner region (40) and being surrounded by the outer frame (39), at least one first passage opening (13 to 16) arranged between the outer frame (39) and the inner frame (43) and separated from the central inner region (40) by a frame wall on a first and/or opposite second frame side of the inner frame (43), and at least one liquid passage (45, 46) provided by the frame wall and configured to distribute a liquid from the first passage opening (13) to a feeding area (40′) and/or to collect a liquid from the feeding area (40) to the first passage opening (16a, 16b)), the feeding area (40′) being aligned with the central inner region (40) but being outside and/or in front of the inner frame (43), wherein the liquid passage extends asymmetrically and/or discontinuously along the first and/or second frame side.

A system for remedying deep-sea mine tailings includes a reaction basin in which the solid-liquid ratio of deep-sea mine tailings is adjusted and into which aluminum sulfate is injected as an additive for extraction of heavy metals from the deep-sea mine tailings.

Implementations of a water filtration system are provided. In some implementations, the water filtration system comprises a housing having a plurality of ports for receiving and outputting fluids wherein the housing encloses components configured to, in a filtration mode, filter water received through one of the plurality of ports to produce potable water and output the potable water through one of the plurality of ports and wherein the housing encloses components configured to, in a flush mode, use fluid received through one of the plurality of ports to remove contaminants captured in the water filtration system and output the contaminants through one of the plurality of ports.

A device for mass transfer between blood and at least one gas/gas mixture, includes first and second chambers through which blood is able to flow and in each of which a respective plurality of mass-permeable hollow fibers are disposed around a respective axially extending core element, wherein a gas/gas mixture is able to flow through, and blood is able to flow around, the hollow fibers, wherein the second chamber follows the first chamber in the blood flow direction, wherein the first and second chambers are disposed next to one another, and in particular disposed spaced apart between the core element center axes thereof, and the two chambers have a connection in an axial end region by which the chamber volumes through which blood is able to flow are connected, and in particular are connected in the direction of the spacing.