Abstract: A two-stage process for upgrading a gaseous stream containing CO2 and H2S in which the gaseous stream and pressurized water are provided to a first stage absorption process in which a portion of the CO2 is absorbed by the pressurized water. The reduced-CO2 gaseous stream and a chemical solvent suitable for absorbing CO2 and H2S are provided to a second stage absorption process in which the H2S and remaining CO2 are removed from the gaseous stream, producing an acid gas stream and an upgraded gaseous stream meeting pipeline-quality specifications.

Abstract: Ozone resistant O2/N2 gas separation membranes comprise a polymer membrane and an ozone reacting component, such as an antioxidant. The antioxidant may be included in the support layer of a composite membrane or included in the entire structure of an asymmetric membrane. The antioxidants in the separation membrane reduce oxidation and deterioration of the actual separation layer of the membrane.

Abstract: Ozone resistant O2/N2 gas separation membranes comprise a polymer membrane and an ozone reacting component, such as an antioxidant. The antioxidant may be included in the support layer of a composite membrane or included in the entire structure of an asymmetric membrane. The antioxidants in the separation membrane reduce oxidation and deterioration of the actual separation layer of the membrane.

Abstract: Recovery of ethylene glycol from dilute aqueous solutions is accomplished by passing the solution over the surface of a porous hydrophobic membrane capable of passing water vapor but not liquid water. The pressure and temperature provide a positive driving force for the movement of water vapor through the membrane to the opposite face where it is removed by condensation or a stream of gas or liquid. Preliminary concentration of the aqueous solutions may be provided by use of reverse osmosis membrane. The method is useful in the reclamation of spent deicing fluid.