Patent classifications
B01D63/021
Artificial lung and method for manufacturing artificial lung
An artificial lung is provided having a plurality of porous hollow fiber membranes for gas exchange, in which the hollow fiber membranes have outer surfaces, inner surfaces forming lumens, and opening portions through which the outer surfaces communicate with the inner surfaces, any one of the outer surfaces and the inner surfaces is coated with a colloidal solution of an antithrombotic material containing a polymer as a main component, and an average particle size of the colloid is at least 1.5 times a diameter of the opening portions of the hollow fiber membranes. An artificial lung is provided that can effectively suppress leakage of blood plasma components after blood circulation (blood plasma leakage).
MEMBRANE FOR BLOOD PURIFICATION
The present disclosure relates to semipermeable membranes which are suitable for blood purification, e.g. by hemodialysis, which have an increased ability to remove larger molecules while at the same time effectively retaining albumin. The membranes are characterized by a molecular retention onset (MWRO) of between 9.0 kD and 14.5 kD and a molecular weight cut-off (MWCO) of between 55 kD and 130 kD as determined by dextran sieving curves and can be prepared by industrially feasible processes excluding a treatment with salt before drying. The invention therefore also relates to a process for the production of the membranes and to their use in medical applications.
Device for cross flow filtration
A whole blood filtration device is provided with a filter membrane separating a feeding volume and a clean side of the filter membrane from each other. The feeding volume communicates with a first feeding side opening and with a second feeding side opening. The filter membrane has pores with a pore size that ensures permeability of the filter membrane to blood plasma/serum and that retains blood cells. The first feeding side opening can be coupled to a first blood pump for feeding blood from the first feeding side opening into the feeding volume so that blood plasma/serum permeates the filter membrane and blood cells, retained by the filter membrane, exit from the feeding volume through the second feeding side opening.
Polymeric whole blood hollow fiber membrane filter medium and use thereof for separating blood plasma/serum from whole blood
A whole blood hollow fiber membrane filter medium is made of a polymeric material having pores of a pore size that ensures permeability to blood plasma or serum but retains blood cells. The whole blood hollow fiber membrane filter medium is used for filtering a whole blood sample so that blood plasma or serum passes through the whole blood hollow fiber membrane filter medium and blood cells are retained. The obtained blood plasma shows no hemolysis.
Membrane for blood purification
The present disclosure relates to semipermeable membranes which are suitable for blood purification, e.g. by hemodialysis, which have an increased ability to remove larger molecules while at the same time effectively retaining albumin. The membranes are characterized by a molecular retention onset (MWRO) of between 9.0 kD and 14.5 kD and a molecular weight cut-off (MWCO) of between 55 kD and 130 kD as determined by dextran sieving curves and can be prepared by industrially feasible processes excluding a treatment with salt before drying. The invention therefore also relates to a process for the production of the membranes and to their use in medical applications.
Assembly for supporting mixed biofilm
A bioreactor has a biofilm that receives a gas through a supporting membrane and another biofilm attached to an inert support. The first biofilm is aerated through the membrane and provides nitrification. The other biofilm has an anoxic or anaerobic zone and provides denitrification. A module useful in the bioreactor has cords potted in at least one potting head. Optionally, some or all of the cords have a gas transfer membrane. The module may provide inert supports, active gas transfer supports or a combination of both types of support. Multiple modules may be assembled together into a cassette, the cassette providing inert supports, active supports or a combination. The module or cassette may have an aerator for mixing or biofilm control.
Hemodialyzer for blood purification
The present disclosure relates to a dialyzer comprising a bundle of semipermeable hollow fiber membranes which is suitable for blood purification, wherein the dialyzer has an increased ability to remove larger molecules while at the same time it is able to effectively remove small uremic toxins and efficiently retain albumin and larger proteins. The invention also relates to using said dialyzer in hemodialysis.
Contact-free thermoforming of fiber bundles
The present disclosure relates to processes for the production of capillary dialyzers. The processes involve contact-free thermoforming of bundles of hollow fiber membranes. The present disclosure also relates to an apparatus for contact-free thermoforming of bundles of hollow fiber membranes.
Composite hollow fiber membrane, manufacturing method therefor, hollow fiber membrane cartridge including same, and fuel cell membrane humidifier
The present invention relates to a composite hollow fiber membrane, a manufacturing method therefor, a hollow fiber membrane cartridge including same, and a fuel cell membrane humidifier, the composite hollow fiber membrane comprising a hollow fiber membrane and a contaminant collection layer coated on the inner surface of the hollow fiber membrane. The composite hollow fiber membrane can prevent performance deterioration of a fuel cell by removing, without a separate gas filtering device, contaminants such as nitrogen oxide (NO.sub.x), sulfur oxide (SO.sub.x), and ammonia (NH.sub.3) during a humidifying process.
OPTIMIZED HEMODIALYZER FOR BLOOD PURIFICATION
The present disclosure concerns a hemodialyzer for the purification of blood and use thereof. The hemodialyzer comprises a bundle of hollow fiber membranes, wherein the hollow fiber membranes have an inner diameter (d.sub.B) within the range of 168-175 m, a fiber wall thickness (.sub.m) within the range of 25-26 m, and an effective length (L) within the hemodialyzer within the range of 207-287 mm. The bundle of hollow fiber membranes has a packing density within the range of 57.5-60.0%, and a total membrane surface area (A.sub.tot) within the range of from 1.64 to 1.73 m.sup.2.