The present invention relates to a filtration device being adapted for continuous vibration and pressure driven filtration. Said filtration device comprises a filter module which comprises at least one tubular semipermeable membrane element, said module further comprises a drain area for permeate, an outlet for permeate, an inlet for feed fluid and an outlet for retentate; said module further comprises one or more flexible volume chambers being filled with gas and in close contact with but separated from the internal module of the filter module through a flexible wall; said filtration device comprises a vibration motor being adapted to provide a vibrating motion to the device.

A method and chemical delivery system and device are provided. One method useful in the present invention includes contacting a non-aqueous hydrazine solution with a carrier gas and/or vacuum and delivering a gas stream comprising hydrazine to a critical process or application. One chemical delivery system and device useful in the present invention includes a non-aqueous hydrazine solution having a vapor phase that is in contact with a process carrier gas and/or vacuum. One device useful in the present invention includes a chamber for containing a liquid comprising at least one volatile process chemical, such as a non-aqueous hydrazine solution, a hydrogen peroxide solution, or another suitable process chemical, in fluid communication with a permeable or semi-permeable membrane from which the volatile process chemical can be drawn using a carrier gas and/or vacuum. Another method useful in the present invention involves drawing a process chemical from a device as a disclosed herein using a process carrier gas or vacuum and delivering the process chemical to a critical process or application. The system further includes a carrier gas and/or vacuum in fluid contact with the vapor phase and an apparatus for delivering a gas stream comprising at least one component of the solution comprising at least one process chemical to a critical process or application.

An ultra-filtration membrane assembly having an exterior housing having a housing; an ultra-filtration membrane provided within the housing, the ultra-filtration membrane being having a plurality of elongated filtration fibers arranged in a spiraled coil; and one or more filaments woven around the plurality of elongated filtration fibers thus binding each of the one or more adjacent elongated filtration fibers at a predetermined axial spacing from one another.

A fluid degassing device includes a first housing, a second housing disposed within the first housing, a first flow circuit defined by the second housing and the first housing between a first flow circuit opening and a second flow circuit opening of the first flow circuit, and a tube bundle of selectively permeable membrane tubes disposed in the first flow circuit between the second housing and first housing. The tube bundle is disposed at least partially around a circumference of the second housing and the first flow circuit is defined between the first flow circuit opening of the first flow circuit and the second flow circuit opening such that fuel flows rotationally around the second housing through the tube bundle.

A fluid degassing device includes a first housing, a second housing disposed at least partially within the first housing, and a first flow circuit defined by the second housing and first housing and the first housing, wherein the second housing includes a second housing opening of the first flow circuit and the first housing includes a first housing opening of the first flow circuit. The device includes a tube bundle of selectively permeable membrane tubes disposed in the first flow circuit between the second housing and first housing. The tube bundle is disposed at least partially around a circumference of the second housing. The tube bundle is configured to be in fluid communication with a second flow circuit to fluidly communicate with an inner channel of the tubes of the tube bundle.

A membrane element includes a central pipe having, in its outer periphery, holes; a membrane wound body in which a membrane member is wound on the central pipe; end members arranged, respectively, at both ends of the membrane wound body; and an exterior member fitted to at least an outer periphery of the membrane wound body. In this element, the exterior member includes a fiber reinforced resin having a reinforcing fiber wound on the outer periphery of the membrane wound body; the end members each includes flexible portions extended from a main body toward the membrane wound body; and the reinforcing fiber is wound also onto an outer periphery of the flexible portions in a state that the flexible portions are deformed toward an outer peripheral surface of the membrane wound body.

A fluid separation apparatus comprising a fluid separation membrane is provided. The fluid separation apparatus comprises a fluid separation membrane extending in one direction and having a cross-section with a closed curve shape, wherein the fluid separation membrane has a thickness of 0.1 mm to 2 mm, and an outer diameter of 60 mm to 360 mm when the cross-section is adjusted to be circular.

A membrane system isolates environment volume, contains hazards, enables detoxification, hazard removal, infrastructure restoration, and substance recovery. The flexible membrane system adjusts to advantageously shape its isolated volume and integrate existing infrastructure. Pollution and hazardous energy, including crude oil, toxic-gas, radioactive fallout, fire, and other hazards are isolated, while concurrently enabling access within the isolated volume. Pod encapsulated and readily deployed, the membrane system operates semi-autonomously, uses selective-filtering, specific gravity and substance differences to channel matter, mitigate hazards, protect the biosphere, preserve infrastructure and capture substances.

A membrane system isolates environment volume, contains hazards, enables detoxification, hazard removal, infrastructure restoration, and substance recovery. The flexible membrane system adjusts to advantageously shape its isolated volume and integrate existing infrastructure. Pollution and hazardous energy, including crude oil, toxic-gas, radioactive fallout, fire, and other hazards are isolated, while concurrently enabling access within the isolated volume. Pod encapsulated and readily deployed, the membrane system operates semi-autonomously, uses selective-filtering, specific gravity and substance differences to channel matter, mitigate hazards, protect the biosphere, preserve infrastructure and capture substances.

Systems and methods for separating a liquid mixture are disclosed. A membrane is first soaked by the liquid mixture via dynamic soaking to reach steady state. During the soaking process, the flow rate of the liquid mixture is increased at a flow rate ramp, the temperature is increased at a temperature ramp, and the pressure drop is increased at a pressure drop ramp. After the soaking process, the liquid mixture is separated by the membrane under optimized conditions to produce a permeate and a retentate.