Abstract: Systems and methods for cleaning and disinfecting a medical therapy device that delivers any one of hemodialysis, hemodiafiltration and hemofiltration. The system has a base module that has at least one segment of a controlled compliant flow path and at least one pair of jumpered ports configured on the base module. One or more components have connections connectable to the jumpered ports of the base module to provide for fluid communication between the segment of the controlled compliant flow path in the base module and a flow path defined by the one or more components. The base module is connected to the one or more components that define a flow path configurable for carrying out in part at least one function performed during any one of hemodialysis, hemodiafiltration or hemofiltration.

Abstract: A device for forming a liquid treatment apparatus includes a main part; and a receiving part including a cavity for receiving a connecting head of a replaceable liquid treatment cartridge having at least one port in liquid communication with an interior of the liquid treatment cartridge such that the at least one port(s) of the connecting head are in sealed liquid communication with corresponding ports of the receiving part. The receiving part is journalled for movement between a first and a second position with respect to the main part whilst the connecting head is inserted in the cavity. The head is insertable into and retractable from the cavity in the first position. The liquid treatment cartridge is lockable to the device by at least moving the receiving part with the inserted connecting head into the second position.

Abstract: A low energy nitrogen removal wetland system is disclosed to provide high rates of nitrogen removal treatment for wastewater with low energy requirements. The wetland system uses down-flow rock-filled wetlands for nitrogen removal. The system has no aeration requirements, thus resulting in low energy consumption. The wetland system comprises a first column receiving drainage influent, a mid-level reservoir, a second column receiving drainage from the mid-level reservoir and a lower level reservoir receiving discharge from the second column. The first and the second columns are filled with media layers comprise rock media with ammonia adsorption capacity for ammonia removal. The wetland system operates in a flood and drain operation mode or a continuous flow mode.

Abstract: A filter element includes a first end cap, a second end cap, and an intermediate end cap disposed between the first end cap and the second end cap. A ring of first filter media circumscribing a first central cavity is disposed between the first end cap and the intermediate end cap. A ring of second filter media is disposed between the intermediate end cap and the second end cap. The filter element also includes an air-bleed conduit axially extending through the first central cavity and comprising a first portion integrally formed with the first end cap and a second portion integrally formed with the intermediate end cap and configured to connect to the first portion thereby forming a conduit for transmitting fluid.

Abstract: A reversible fluid filtration system includes a receiver unit and a fluid filtration unit. The receiver unit has a first side and second side with a fluid channel therebetween. The fluid filtration unit includes filter media positioned between a first end and a second end. Openings in the first end are fluidly connected with the openings in the second end via the filter media. The first end and second end are independently attachable to the receiver unit via the second side. Attachment of the filtration unit first end to the receiver unit allows filtration of fluid entering the receiver unit fluid channel. Attachment of the filtration unit second end to the receiver unit allows fluid entering the receiver unit to remove solid material from the filter media and recharge the filter media.

Abstract: The fuel filter (1) contains a filter element (4) and an additive tank (13) in a housing (2, 3). The filter element is engaged against the removable cover (3) of the housing and has a filter medium (5) extending in an annular manner around an inner space (9). An additive release device (32) extends into this inner space (9) to distribute liquid additive from the tank (13) into a fuel circulation circuit for an internal combustion engine. The additive selectively flows into a sealed distribution channel (DC) of the device (32) depending on an open or closed configuration of an actuator component (62) associated with the distribution channel. The distribution channel (DC) opens into a fuel channel (52) of the cover (3) that has a larger cross-section than the distribution channel (DC).

Abstract: A fuel filter device is disclosed. The fuel filter device has a first member that includes a main body tubular portion and a first connection tubular portion for connecting the first member to a fuel pipe. The main body tubular portion includes a flow channel cross-section greater than that of the first connection tubular portion. The main body tubular portion includes a first end portion and a second end portion. The first connection tubular portion is disposed on the first end portion. An opening is provided through the second end portion. A filter element portion is accommodated in the main body tubular portion. A second member includes a lid portion and a second connection tubular portion for connecting the second member to a fuel pipe. The lid portion covers the opening of the main body tubular portion.

Abstract: A water or wastewater treatment process that includes a dissolved air flotation process for removing suspended solids from influent water or mixed liquor. In one process, the dissolved air flotation process is carried out in the absence of adding a coagulant or a flocculant, but yet produces TSS removal efficiencies comparable to those achieved by conventional dissolved air flotation processes that employ a coagulant and a flocculant. In other processes, a coagulant and/or a flocculant is added directly to the mixing zone of a dissolved air flotation system or is added via a pressurized white water injection system. In another process, the use of a coagulant and a flocculant is useful in removing TSS and reducing the concentration of phosphorus in the water being treated.

Abstract: Systems and methods for cleaning and disinfecting a medical therapy device that delivers any one of hemodialysis, hemodiafiltration and hemofiltration. The system has a base module that has at least one segment of a controlled compliant flow path and at least one pair of jumpered ports configured on the base module. One or more components have connections connectable to the jumpered ports of the base module to provide for fluid communication between the segment of the controlled compliant flow path in the base module and a flow path defined by the one or more components. The base module is connected to the one or more components that define a flow path configurable for carrying out in part at least one function performed during any one of hemodialysis, hemodiafiltration or hemofiltration.

Abstract: Micro-channel fluid filters and methods of use are provided herein. In one embodiment a fluid film may include a plurality of dividing walls extending from an upper surface of a film, the plurality of dividing walls forming a plurality of tapered inlet channels, a plurality of cross channels formed along a length of each of the plurality of dividing walls, an inlet channel for each of the plurality of tapered inlet channels, and an outlet channel for each of the plurality of tapered inlet channels.

Abstract: The disclosure relates to a system and method for cleaning filters, such as membrane filters. More particularly, a method and system are disclosed for retaining a plurality of small particulates, preferably in the shape of beads, which contact sludge or other despots on the membrane filters to remove unwanted debris that would otherwise form on the cleaning filters. In various embodiments, the plurality of small particulates are retained in a permeable enclosure formed of wedgewire.

Abstract: A filtration container assembly generally includes an outer container having a first end and a second end and defining an inner cavity, and a plunging assembly configured to be received within the outer container inner cavity, wherein the plunging assembly includes an inner sleeve having a first end and a second end and an outer wall defining an inner bore, wherein the outer wall is continuous from the first end to the second end, and a filtration assembly coupled to the inner sleeve at the second end.

Abstract: Disclosed herein is a process for carrying out an ion exchange process which involves providing two interacting sets of banks of continuously stirred tank reactors (CSTR's) each containing a bed of ion exchange resin and causing the resin to move in one direction through each bank of reactors and the feed solution and/or or eluant in the opposite direction. In carrying out the process, a feed solution is introduced in a first reactor causing dissolved ions to be captured on the resin, eluant is introduced into a reactor upstream of the first reactor in the direction of resin movement causing ions captured on the resin to be removed into the eluant and eluant rich in ions removed from the resin will be taken from a reactor upstream of the reactor in which the eluant was introduced, for further processing.

Abstract: In a filter cartridge (CC) for a fuel filter, the filter element (4) and the additive module are connected and typically stacked so as to allow them to be integrally inserted into a filter housing. The substantially annular filter medium (5) delimits an inner space (9) into which at least one part (24) of the attachment end of the additive module can be engaged. The liquid additive is stored in a casing forming a tank (13) that is placed at a fuel pressure and delimits an internal volume (V2) that can be varied so as to maintain an identical pressure between the liquid additive and the fuel at the periphery (V3) of the tank (13). The additive module has an external connection (28) with a liquid additive outlet pipe (12a), said external connection (28) including sealing means (37, 38) for automatically closing the outlet pipe in a fluidtight manner when the external connection is in a disengaged state.

Abstract: Aspects of embodiments relate to a method for treating water received at a treatment system. The method may include reducing the hardness of the water by subjecting the water to electrolysis by an electrolytic hardness reducer; and substantially removing disinfectant from the water by irradiating the water with ultraviolet light by a UV disinfectant reducer. The method may further include sanitizing the electrolytic hardness reducer and/or sanitizing the UV disinfectant reducing apparatus by running hot water through either one or both of them.

Abstract: Composite ion-exchange materials for use in an ion-exchange column are provided. Also provided are ion-exchange columns packed with the materials and methods for using the materials to remove metal ions from samples, such as waste water samples. The composite ion-exchange materials comprise a composite material comprising a metal chalcogenide and an alginate, wherein the composite material is mixed with a granular material.

Abstract: The water treatment system, particularly pre-filtration unit of the water treatment system, comprising at least one chlorine sensor device, includes a salt-water treatment device which is connected to the chlorine sensor device, an electrolysis cell being disposed in the associated line, and thereafter a pump and a release valve.

Abstract: A method of operating an extracorporeal blood treatment includes, prior to commencing an extracorporeal blood treatment, reading from a storage device (4a, 5a) stored values of a patient-specific prescription parameter. These stored values relate to a sequence of previous extracorporeal blood treatments. In addition, the method includes processing the stored values of the parameter read from the storage device (4a, 5a) according to a predetermined algorithm to determine a current value of the patient-specific prescription parameter. The current value is then available for the subsequent extracorporeal blood treatment.

Abstract: A renal therapy apparatus includes a blood filter, a blood pump, a treatment fluid pump, and a control unit configured to control at least one of the blood pump or the treatment fluid pump during a filter cleaning sequence. In a first phase of the filter cleaning sequence, a first fluid including a blood-compatible and physiologically safe fluid is transferred back and forth across the insides and/or outsides of the blood filter. After the first phase, a second fluid is formed by mixing the first fluid with air. In a second phase of the filter cleaning sequence, the second fluid is transferred across the insides and/or outsides of the blood filter at least one time.

Abstract: A process of treating water includes a membrane separation stage and a deionization stage separating raw water into a first concentrate stream and permeate stream, the first concentrate stream is separated at least in part into a second concentrate stream and permeate stream, the first permeate stream is fed into a diluate chamber from which it exits again as a product stream, the second permeate stream is fed into a downstream electrodeionization appliance from which it exits as a third concentrate stream, and the second and the third concentrate streams are degassed and added to the raw water stream before the stream is fed into the membrane separation stage.