Abstract: A gas recovery system comprising a source of gas having a preselected concentration of a desired component (9), at least one application (1) that adds impurities to said gas, and at least one an adsorption system (6) that purifies said gas to produce a purified gas for re-use in application (1), wherein said at least one adsorption system includes at least one adsorbent bed (A) having at least three layers of adsorbents. A recovery process is also disclosed.

Abstract: The present invention relates to a gas recycling system that includes a) a source of gas having a predetermined purity; b) an application system that uses the gas and adds contaminants to the gas; c) an adsorption system for removing the contaminants from the gas to produce a purified gas and a waste gas; d) a gas purity analyzer for measuring the amount of the contaminants in the waste gas; and e) conduits connecting the gas source to the application system, and the application system to the adsorption system.

Abstract: This invention is directed to a three-stage process for recovering and purifying a helium gas, and a system for using the three-stage process. The steps comprise a) introducing a gas from a cold spray forming chamber to a particulate removing apparatus to form a particulate-free helium gas, and recycling a first portion of the particulate-free helium gas back to the chamber; b) passing a second portion of the particulate-free helium gas to a first compressor prior to passing a helium gas purification membrane to form a purified helium gas and an exhaust gas, and passing the purified helium gas to mix with the first portion of particulate-free helium gas to the chamber; and c) passing a third portion of the particulate-free helium gas to a liquid separator apparatus to remove water and a receiver to dampen any pulsations to form a liquid-free helium gas, and recycling the liquid-free helium gas to said cold spray forming chamber.

Abstract: A gas recovery system comprising a source of gas having a preselected concentration of a desired component (9), at least one application (1) that adds impurities to said gas, and at least one an adsorption system (6) that purifies said gas to produce a purified gas for re-use in application (1), wherein said at least one adsorption system includes at least one adsorbent bed (A) having at least three layers of adsorbents. A recovery process is also disclosed.

Abstract: The invention comprises a gas recycling system comprising: a) a source of gas having a predetermined purity (28); b) an application system (6) that uses said gas and adds contaminants to said gas; c) an adsorption system (1) for removing said contaminants from said gas to produce a purified gas, and a waste gas; d) a gas purity analyzer (100) for measuring the amount of said contaminants in said waste gas; e) conduits ((5), (8), (9) (13) and (15) connecting the gas source (4) to said application system, said application system (6) to said adsorption system.

Abstract: This invention is directed to a three-stage process for recovering and purifying a gas, and a system for using the three-stage process. The steps comprises a) introducing a gas from a chamber to a particulate removing apparatus to form a particulate-free gas, and recycling a first portion of the particulate-free gas to the chamber; b) passing a second portion of the particulate-free gas to a first compressor prior to passing a selective gas purification membrane to form a purified gas and an exhaust gas, and passing the purified gas to mix with the first portion of particulate-free gas to the chamber; and c) passing a third portion of the particulate-free gas to a liquid separator apparatus and a receiver to form a liquid-free gas, and recycling the liquid-free gas to said chamber.

Abstract: This invention is directed to a three-stage process for recovering and purifying a helium gas, and a system for using the three-stage process. The steps comprises a) introducing a gas from a cold spray forming chamber to a particulate removing apparatus to form a particulate-free helium gas, and recycling a first portion of the particulate-free helium gas back to the chamber; b) passing a second portion of the particulate-free helium gas to a first compressor prior to passing a helium gas purification membrane to form a purified helium gas and an exhaust gas, and passing the purified helium gas to mix with the first portion of particulate-free helium gas to the chamber; and c) passing a third portion of the particulate-free helium gas to a liquid separator apparatus to remove water and a receiver to dampen any pulsation to form a liquid-free helium gas, and recycling the liquid-free helium gas to said cold spray forming chamber.

Abstract: A process for producing atomized powder, such as a metal powder, using a recirculating atomization gas, such as helium, and the apparatus used for producing the atomized powder

Abstract: Apparatus and process for recycling a quenching gas, such as helium, to be used with a treating gas, such as a carburizing gas, for the treating of components in an atmospheric furnace.

Abstract: A cryogenic rectification system comprising an upstream krypton/xenon knockout column and a downstream oxygen upgrader column wherein the knockout column processes a crude feed for removal of heavy components including hydrocarbons and the upgrader column produces ultra high purity oxygen.

Abstract: A.

Abstract: A process for producing an overbased oil soluble calcium sulfonate, comprising the steps of: (a) mixing a substrate comprising a sulfonic acid or a calcium salt of a sulfonic acid, with at least one alcohol, a diluent oil, a carboxylic acid, an acidic material, water and calcium oxide to form a mixture; (b) heating the mixture to its reflux point to form a neutral calcium salt of the acid moieties; (c) removing a substantial portion of distillable solvents to form an intermediate residue; (d) adding to the intermediate residue at least one alcohol, a surfactant, calcium oxide and water such that for every 100 parts of substrate, there are not more than 25 parts water to form an intimate mixture having a direct base number of 90-250; (e) heating said intimate mixture (d) to below its reflux point to form a heated intimate mixture; (f) passing gaseous carbon dioxide into the heated intimate mixture (e) to form an overbased calcium sulfonate and a mixture of calcium hydroxide, calcium carbonate and regenerated w