Abstract: This invention relates to a dual-layer, multifunctional hollow fiber membrane having at least two layers that perform two respective functions: 1) a layer that performs a separative function separating a solvent such as a liquid or gas from its solute species; and 2) a layer that performs the function of generating a magnetic field. The layer generating the magnetic field preferably has magnetic nano or micro particles embedded therein to attract, capture and/or position paramagnetic draw solute particles to maximize their osmotic effect.

Abstract: A forward or pressure retarded osmosis system using submerged hollow fiber membranes, a draw solution of superparamagnetic nanoparticles (preferably an iron oxide core with a silica shell that is chemically treated with a dispersant stabilizing it in a permanent suspension), that produces an osmotic pressure that drives fluid through the semipermeable membrane and a multiplicity of rigidly connected, permanent ring magnets forming layers, that maintains the locational position of the magnetic nanoparticles inside the hollow fiber membranes, preventing the draw solute particles from leaving membrane surface area. The various magnetic fields produced by the ring magnets attract the magnetic nanoparticles toward the surface area of the membrane preventing dilutive concentration polarization, thereby maximizing permeate flux rate.

Abstract: This invention is an onboard pressure retarded osmosis (PRO) unit for charging or recharging the battery of an electric conveyance or for feeding the conveyance's motor directly. The PRO unit exploits the combined use of osmotic pressure, a water-submerged hollow fiber membrane system, a concentrated aqueous solution of superparamagnetic nanoparticles (a ferrofluid) as a draw solution, and a solenoid-type permanent magnetic field, to create a high pressure water flow that acts upon one or more hydroturbine generators to produce electricity. After the pressurized water acts upon the hydroturbine generators, it is returned to the feed side of the membrane system to once again become permeate, in effect making the entire system a closed loop, continuously re-circulating process. The membrane cells may be heated to increase power density.

Abstract: An array of hollow fiber membranes is grouped into bundles is submerged in an enclosed pure-water bath. The bundles are potted into top and bottom membrane headers such that the fiber lumen (the inside of the hollow fiber) is open to the inside of the membrane header and the pure feedwater is prevented from leaking into either the header or into the inside of a hollow fiber. Pure water penetrates the hollow fiber membrane. In accordance with pressure retarded osmosis (PRO) principles, the permeate and draw solution within the lumen are transported to at least one hydroturbine where electricity is generated. The draw solution contains superparamagnetic nanoparticles that are prevented from proceeding beyond a magnetic field. The system has a heater to improve its efficiency.

Abstract: A forward osmosis system using submerged hollow fiber membranes, a draw solution of superparamagnetic nanoparticles (preferably an iron oxide core with a silica shell that is chemically treated with a dispersant stabilizing it in a permanent suspension), that produces an osmotic pressure that drives fluid through the semipermeable membrane and a magnetic field produced by either a permanent magnet or solenoid-type electromagnet that is applied to either separate and reuse or to prevent the movement of the magnetic nanoparticles away from the membrane surface area. Since forward osmosis is independent of both the type of membrane (hyper, nano, ultra, or micro) and the fluid type (the fluid being processed can be oil or water-based), it can be widely applied to many fluid processes within the water treatment (wastewater treatment, demineralizing industrial cooling water, and seawater desalination) and non-water treatment industries such as the food and beverage, medical, and chemical industries.

Abstract: A mercury remediation method and apparatus for reducing mercury levels in water to a nanogram per liter level that uses four treatment steps: (1) chelation; (2) oxidation; (3) reduction; and (4) air stripping, vapor/liquid separation. There is a fifth step in the process, which does not involve the wastewater. It is to scrub the stripper air of the volatile mercury in an off-gas adsorption unit or to condense volatile mercury in a cryogenic mercury trap.