A hollow fiber membrane fluid transport device is disclosed wherein the fibers are comprised of Polytetrafluoroethylene (PTFE), and the potting materials are comprised of fluorocopolymer and or fluoroterpolymer based materials. The potting of the device utilizes a compressed chemically resistant fluorocopolymer and or fluoroterpolymer film, allows for ease of manufacture without destruction of the PTFE hollow fibers, with high packing densities, and without the processing complexity of pre-melting, extruding, or chemical crosslinking of any polymeric adhesives. Furthermore, the PTFE hollow fibers can be treated with a fluoropolymeric solvent solution before the chemically resistant film is applied to enhance the adhesion of the PTFE fiber to the film. PTFE hollow fibers, and its respective fluoro-co and terpolymers as potting films impart high packing densities, superb chemical resistance and temperature resistance without membrane contamination, or low fiber pull strength, as is sometimes observed with standard potting materials such as polyurethane and epoxy.

A hollow fiber membrane fluid transport device is disclosed wherein the fibers are comprised of Polytetrafluoroethylene (PTFE), and the potting materials are comprised of fluorocopolymer and or fluoroterpolymer based materials. The potting of the device utilizes a compressed chemically resistant fluorocopolymer and or fluoroterpolymer film, allows for ease of manufacture without destruction of the PTFE hollow fibers, with high packing densities, and without the processing complexity of pre-melting, extruding, or chemical crosslinking of any polymeric adhesives. Furthermore, the PTFE hollow fibers can be treated with a fluoropolymeric solvent solution before the chemically resistant film is applied to enhance the adhesion of the PTFE fiber to the film. PTFE hollow fibers, and its respective fluoro-co and terpolymers as potting films impart high packing densities, superb chemical resistance and temperature resistance without membrane contamination, or low fiber pull strength, as is sometimes observed with standard potting materials such as polyurethane and epoxy.

A purification system for a colloidal dispersion containing an unwanted dissolved substance in the dispersing liquid phase is described which includes a back-pressure regulating feature, disposed in a first conduit and downstream of a semi-permeable filter element. This is used to force a portion of the unpurified dispersing liquid across the filter element and into a second conduit. The second conduit is associated with an adsorptive element that serves to remove the unwanted dissolved substance from the filtered portion of the dispersing liquid. A mixing chamber is disposed downstream of the back-pressure regulating feature whereby the purified dispersing liquid portion from the second conduit rejoins the bulk flow of the colloidal dispersion passing through the first conduit. In a preferred embodiment, hollow fibers are used which serve as the back-pressure regulating feature, the adsorptive element, and the mixing chamber before being discharged at the outlet of the device.

There is provided a hollow fiber membrane module including a cylindrical case having at least a discharge port for raw water in a side face thereof; a fixing member to which open ends of a large number of hollow fiber membranes forming a hollow fiber membrane bundle housed inside the cylindrical case are fixed; and a flow straightening cylinder which is provided between the discharge port for the raw water and an outer periphery of the hollow fiber membrane bundle, which is fixed to the fixing member, and which has a plurality of flow straightening holes. The flow straightening cylinder includes a large inner diameter portion and a small inner diameter portion and the small inner diameter portion is mounted to the fixing member with a lower face of the fixing member positioned at the small inner diameter portion.

A water purifier, including a housing, a piston cylinder, a base, and a dust cap. The housing includes a water inlet end and a water outlet end, and a composite filter material and an ultrafiltration membrane are disposed in the housing to constitute a filter element. The piston cylinder is sleeved on the housing. The upper end of the piston cylinder is provided with a suction nozzle. The base includes an upper part and a lower part. The upper part includes a lower bayonet and an upper bayonet. The lower part includes a multipurpose interface and a water inlet nozzle. The dust cap is disposed on the upper end and covers the suction nozzle. The central part of the dust cap protrudes downward to form a flexible sealing plug. The water inlet end of the housing is secured to the lower bayonet of the base.

A hollow fiber membrane filtration device includes a housing, a hollow fiber membrane module, a supporting tube, and a bottom cover. The housing includes a top wall having a positioning hole intercommunicating with a receiving space of the housing. The hollow fiber membrane module includes a plurality of densely arranged inverted U-shaped hollow fibers. The hollow fiber membrane module is inserted upward through a bottom opening of the housing into the receiving space. The supporting tube is inserted in the fiber membrane seat and extends upright to couple with the top wall of the housing. The supporting tube can be coupled with a filtration seat and a fixing rod which are currently available. The bottom cover is coupled to the bottom opening and includes a flow guiding space having an upwardly facing opening. The bottom cover includes an outlet spaced from the central hole of the supporting tube.

Disclosed herein is a perfusion filtration module or bioreactor for filtering a fluid, wherein the filtration module or bioreactor has a plurality of hollow fiber filter membranes that are splayed to reduce fouling of the filtration array.

A water filter cartridge is reduced in fluctuation in filtration flow rate or in filtration performance due to activated carbon, and can exhibit stable performance even at the time of large scale production; and a water purifier is equipped with the water filter cartridge. A water filter cartridge having particulate activated carbon filled in a case for accommodating a filtering material in which the ratio of the total mass of particulate activated carbon having a particle size of 0.3 to 4.0 mm relative to the total mass of activated carbon is 97% by mass or more, and, in a particle size distribution which represents the relationship of the mass ratio of activated carbon relative to the particle size of activated carbon, a peak at which the mass ratio is 31% by mass or more does not appear in a particle size range of from 0.3 to 4.0 mm.

A cell culture bioreactor has perfusion membranes and gas transfer membranes or a gas phase in an extra-membrane space in contact with a film on the perfusion membranes. Gas transfer membranes may travel through the perfusion membranes or through the extra-membrane space. Examples with hollow fiber and flat sheet membranes are shown. One or more of the membranes optionally has a responsive surface, for example a thermo-responsive surface. In some examples, membranes are located in X-Y planes while the length of the reactor extends in a Z-direction.

A cell culture bioreactor has perfusion membranes and gas transfer membranes or a gas phase in an extra-membrane space in contact with a film on the perfusion membranes. Gas transfer membranes may travel through the perfusion membranes or through the extra-membrane space. Examples with hollow fiber and flat sheet membranes are shown. One or more of the membranes optionally has a responsive surface, for example a thermo-responsive surface. In some examples, membranes are located in X-Y planes while the length of the reactor extends in a Z-direction.