The present invention belongs to the technical field of membranes and provides a carbon nanotube/nanofiber conductive composite membrane and a preparation method thereof. The conductive membrane with a meshy pore structure intertwined by one-dimensional nano materials is constructed by taking one-dimensional nanofiber nonwovens prepared by electrospinning as a support layer and CNTs cross linked on the support layer as a separation layer. The membrane pore size of the composite membrane involved can be controlled from microfiltration to ultrafiltration, and membrane morphology includes flat membranes, hollow fiber membranes, and spiral-wound membranes. The main advantages and beneficial effects of the composite membrane involved are: simple preparation steps, better permeability and mechanical strength, good hydrophilicity and electrical conductivity, and easy mass production and application.

The present invention belongs to the technical field of membranes and provides a carbon nanotube/nanofiber conductive composite membrane and a preparation method thereof. The conductive membrane with a meshy pore structure intertwined by one-dimensional nano materials is constructed by taking one-dimensional nanofiber nonwovens prepared by electrospinning as a support layer and CNTs cross linked on the support layer as a separation layer. The membrane pore size of the composite membrane involved can be controlled from microfiltration to ultrafiltration, and membrane morphology includes flat membranes, hollow fiber membranes, and spiral-wound membranes. The main advantages and beneficial effects of the composite membrane involved are: simple preparation steps, better permeability and mechanical strength, good hydrophilicity and electrical conductivity, and easy mass production and application.

A hydrogen-selective membrane including a metal leaf applied to a substrate. A system and method for fabricating a hydrogen-selective membrane, including applying a metal leaf to a substrate, annealing the metal leaf, applying a hydrogen-permeable metal to the annealed metal leaf on the substrate, and annealing the hydrogen-permeable metal and the annealed metal leaf to give an alloy of the hydrogen-permeable metal and the metal leaf. A system and method for repairing a hydrogen-selective membrane having defects including applying a metal leaf to an external surface of membrane material of the hydrogen-selective membrane, annealing the metal leaf and metal of the membrane material to form an alloy of the metal leaf and the metal to repair the defects.

A hydrogen-selective membrane including a metal leaf applied to a substrate. A system and method for fabricating a hydrogen-selective membrane, including applying a metal leaf to a substrate, annealing the metal leaf, applying a hydrogen-permeable metal to the annealed metal leaf on the substrate, and annealing the hydrogen-permeable metal and the annealed metal leaf to give an alloy of the hydrogen-permeable metal and the metal leaf. A system and method for repairing a hydrogen-selective membrane having defects including applying a metal leaf to an external surface of membrane material of the hydrogen-selective membrane, annealing the metal leaf and metal of the membrane material to form an alloy of the metal leaf and the metal to repair the defects.

A blood treatment method includes the steps of inducing flow of a patient's blood through an extracorporeal device inlet and outlet in fluid connection to the circulatory system of the patient. Metastatic DNA contained within patient blood can be rendered non-oncogenic by passing patient blood over a biochemical reactor surface having attached or immobilized DNase 1 enzyme, with the biochemical reactor being contained within the extracorporeal device. The treatment method is performed without adding any chemicals to the blood of the patient.

A blood treatment method includes the steps of inducing flow of a patient's blood through an extracorporeal device inlet and outlet in fluid connection to the circulatory system of the patient. Metastatic DNA contained within patient blood can be rendered non-oncogenic by passing patient blood over a biochemical reactor surface having attached or immobilized DNase 1 enzyme, with the biochemical reactor being contained within the extracorporeal device. The treatment method is performed without adding any chemicals to the blood of the patient.

A flue gas extraction system provides extraction, collection, cooling, enriching and distributing flue gas from a vent stack of a stationary flue gas generator to carbon dioxide consuming crops, orchards, and other photosynthetic organisms. The collected flue gas is processed through the system to achieve optimal temperature, pressure, flowrate, water content and carbon dioxide concentration for application to plants for increasing plant productivity and sequestering the carbon dioxide. The gas distribution network may have one or more membrane modules which receive a low pressure gas mixture, where the membrane modules are utilized to enrich the CO2 concentration and to separate out a nitrogen rich component from the flue gas. Application of carbon dioxide may be supplemented by providing additional components to the plants which maintain a level of fertilization and irrigation suitable for the increased biomass and water utilization efficiency of the plants resulting from the increased intake of carbon dioxide.

A flue gas extraction system provides extraction, collection, cooling, enriching and distributing flue gas from a vent stack of a stationary flue gas generator to carbon dioxide consuming crops, orchards, and other photosynthetic organisms. The collected flue gas is processed through the system to achieve optimal temperature, pressure, flowrate, water content and carbon dioxide concentration for application to plants for increasing plant productivity and sequestering the carbon dioxide. The gas distribution network may have one or more membrane modules which receive a low pressure gas mixture, where the membrane modules are utilized to enrich the CO2 concentration and to separate out a nitrogen rich component from the flue gas. Application of carbon dioxide may be supplemented by providing additional components to the plants which maintain a level of fertilization and irrigation suitable for the increased biomass and water utilization efficiency of the plants resulting from the increased intake of carbon dioxide.

A separation membrane module may decrease a bending load applied to a support member supporting ends of tubular separation membranes and omission of a seal member between the outer circumferential surface of the support member and the inner circumferential surface of a housing. The separation membrane module may include a tubular housing, tubular separation membranes arranged in a longitudinal direction of the housing, end tubes connected to lower ends of the tubular separation membranes, a support box supporting the end tubes, and a backpressure chamber below the support box. The tubular separation membranes may be in communication with a support box collection chamber. A nozzle disposed on the support box may extract permeated fluid. A chamber and the backpressure chamber are in communication via a gap between the support box outer circumferential surface and the inner circumferential surface. The chamber and backpressure chamber have substantially the same pressure.

A separation membrane module may decrease a bending load applied to a support member supporting ends of tubular separation membranes and omission of a seal member between the outer circumferential surface of the support member and the inner circumferential surface of a housing. The separation membrane module may include a tubular housing, tubular separation membranes arranged in a longitudinal direction of the housing, end tubes connected to lower ends of the tubular separation membranes, a support box supporting the end tubes, and a backpressure chamber below the support box. The tubular separation membranes may be in communication with a support box collection chamber. A nozzle disposed on the support box may extract permeated fluid. A chamber and the backpressure chamber are in communication via a gap between the support box outer circumferential surface and the inner circumferential surface. The chamber and backpressure chamber have substantially the same pressure.