An environmental control system includes an air conditioning subsystem and a contaminant removal subsystem downstream of the environment to be conditioned. The contaminant removal subsystem includes: a first gas-liquid contactor-separator; a second gas-liquid contactor-separator; and a dehumidifier disposed either upstream of the first gas-liquid contactor-separator or downstream of the second gas-liquid contactor-separator.

The present disclosure relates to synthetic membranes for the removal, isolation or purification of substances from a liquid, comprising at least one hydrophobic and at least one hydrophilic polymer, wherein 5-40 wt.-% of particles having an average particles size of between 0.1 and 15 μm are entrapped and wherein the membrane has a wall thickness of below 150 μm. Further disclosed are methods for preparing such membranes in various geometries and their use for the adsorption, isolation and/or purification of substances from a liquid.

The present invention relates to synthetic membranes and use of these synthetic membranes for isolation of volatile organic compounds and purification of water. The synthetic membrane includes a hydrophobic polymer layer located on a polymeric membrane support layer. The invention includes a method of isolating volatile organic compounds with the synthetic membrane by contacting a volatile organic mixture with the hydrophobic polymer layer of the synthetic membrane and removing volatile organic compounds from the polymeric membrane support layer of the synthetic membrane by a process of pervaporation. The invention also includes a method of purifying water with the synthetic membrane by contacting an ionic solution with the hydrophobic polymer layer of the synthetic membrane and removing water from the polymeric membrane support layer of the synthetic membrane by a process of reverse osmosis. The invention also relates to methods of isolating non-polar gases by gas fractionation.

Embodiments of the present invention relate to a nanofiltration composite membrane for use to purify water, the methods for preparing said nanofiltration composite membranes and to the nanofiltration composite membranes prepared accordingly.

Disclosed is a nanoporous membrane including a porous support layer and a selective layer. The selective layer, being deposited on a surface of the porous support layer, has an effective pore size smaller than that of the porous support layer and contains an array of polymeric nanoparticles that have on their surfaces a plurality of —C(═O)XR groups. Also disclosed are methods of fabricating a nanoporous membrane described above and using the nanoporous membrane for separating a mixture that contains two solutes.

The present disclosure relates to a method for treating a solvent in wastewater generated in a polycarbonate production process. More specifically, the present disclosure relates to a method for treating a solvent in wastewater generated in a polycarbonate production process, which can easily recover a high purity solvent regardless of the concentration of the solvent by using a membrane distillation method to reuse it, and contribute to energy savings.

A water-permeable device. The device has a supporting layer and a water-permeable membrane. The water-permeable membrane includes graphene layers that are aligned to form interlayer hydrophobic channels between the graphene layers. The interlayer hydrophobic channels are positioned to be aligned with the direction of water permeation. Also disclosed are systems and methods for water treatment.

Systems and methods for separating organic chloramines and inorganic chloramines from an aqueous solution. Such a method includes providing a first container containing an aqueous solution that includes organic and inorganic chloramines and free chlorine, providing a second container containing a trapping solution and a tubular hydrophobic membrane through which inorganic chloramines contained in the aqueous solution can diffuse into the trapping solution, pumping the aqueous solution from the first container through the tubular hydrophobic membrane of the second container; and collecting the aqueous solution pumped through the tubular hydrophobic membrane in a third container connected to the tubular hydrophobic membrane. After pumping is completed, the second container contains an aqueous solution containing the inorganic chloramines and the third container contains an aqueous solution containing the organic chloramines and the free chlorine.

A desalination apparatus is disclosed which comprises: a first tank for storing seawater to be desalinated; a second tank comprising a hydrophobic membrane desalination module operable to absorb only fresh water vapors and reject salt components when the seawater is heated to a first predetermined temperature that changes the seawater into the fresh water vapors, and wherein the hydrophobic membrane desalination module is configured to continuously allow the distilled fresh water to make contact with the fresh water vapors within its interior hollow volume; and a third tank, in fluid communication with the second tank, configured to cause the fresh water vapors from the hydrophobic membrane desalination module to be condensed into liquid fresh water by continuously allowing the fresh water vapors to make contact with a coolant water at a second temperature.

The invention relates to a device for dispensing an aqueous liquid through an interface membrane made partially hydrophilic and partially hydrophobic, made so that when in operation, during each operation of dispensing a metered amount of liquid, the streams of air and liquid flow alternately in a capillary channel (18) downstream from the membrane. Said interface membrane (7) is made of a filtering material which includes biocidal metal cations in the body thereof. Said device comprises a porous insert (8), which is permeable both to liquid and to air, which is arranged upstream from the membrane in the path of the fluids and which is made of a material including sites with negative charges capable of attracting biocidal metal cations from said membrane.