The Boc Group, Inc.

Sidney S Stern

Ravi Kumar Jain

Ravi Kumar

Satish S Tamhankar

Robert A Mostello

Divyanshu R Acharya

Anish Mehta

Temperature rise during the exothermic reduction of nitrogen oxides contained in a carbon dioxide-rich gas stream to nitrogen by contacting the gas stream with ammonia in a reactor containing a reduction catalyst is controlled by recycling a portion of the gaseous effluent from the reactor to the gas stream prior to its introduction into the reactor, thereby cooling the reactor contents without diluting the carbon dioxide in the effluent.

Removal of nitrogen oxide from gas streams

Petrochemicals are produced by the vapor phase reaction of a hydrocarbon with air in the presence of a suitable catalyst. The petrochemical product is removed from the product gas stream, and part or all of the remaining gas stream is passed through a bed of hydrophobic adsorbent, which adsorbs mainly the unreacted hydrocarbon from the gas stream without adsorbing water vapor. The adsorbed hydrocarbon is purged from the bed with air, and the air-hydrocarbon mixture is recycled to the partial oxidation reactor.

Process for the production of petrochemicals

A method and apparatus of separating air in which the air is rectified wig a single column nitrogen generator which produces a nitrogen stream which is expanded into a refrigerant stream and then taken as a medium pressure product. Oxygen enriched air can be taken as low pressure and medium pressure enriched air products. A stream of oxygen enriched air can be used to regenerate the pre-purification unit and also taken as a wet product.

Air separation method and apparatus

High purity argon is produced by subjecting a two-phase liquid-vapor mixture containing up to 3 volume % of nitrogen and/or up to 5 volume % oxygen to cryogenic temperature swing adsorption in an adsorption bed containing one or more adsorbents selective for nitrogen and/or oxygen at a temperature between the bubble point and the dew point of the two-phase mixture.

Purification of fluids by adsorption

A method of rectifying a multicomponent mixture by pressure swing adsorption to separate primary and secondary components of the mixture. Two groups of adsorbent beds are used in the method and adsorbent beds of the two groups are employed in a paired relationship and subjected to feed, co-current depressurization, evacuation, and countercurrent repressurization stages. In the feed stages, pairs of the adsorbent beds are pressurized with the mixture to adsorb the primary component in a first group of the adsorbent beds and in an entry section of a second group of the adsorbent beds. Also during the feed stage, the secondary component is adsorbed in the second group of adsorbent beds in remaining sections thereof. During co-current depressurization, any of the secondary component adsorbed in the first group of adsorbent beds and part of the primary component is driven to the second group of adsorbent beds. The adsorbent beds are individually evacuated to produce primary and secondary product streams rich in the primary and secondary components, respectively. Countercurrent repressurization is effected with a waste stream comprising the effluent from the feed stage. The countercurrent repressurization stage functions to bring the adsorbent beds back up to operating pressure and to drive the primary component back into the first group of adsorbent beds.

Pressure swing adsorption process for fractionating a multi-component

A cryogenic rectification method for producing a product stream from a gaseous mixture having higher and lower volatility components and heavy impurities. In accordance with the method, the mixture is separated by a cryogenic rectification process employing one or more columns having plates, trays or packing for intimately contacting ascending vapor and descending liquid streams within the column. The mixture to be separated after having been compressed is combined with the recycle stream to produce a combined stream which is purified in a prepurification unit that is designed to remove the heavy contaminants. The combined steam is divided into major and minor streams. The major stream is then cooled and separated into liquid and vapor phases. Heavy impurities concentrate in the liquid phase taken as the recycle stream, which is then pumped to a high enough pressure for vaporization of the impurities. The resulting vapor is then reduced in pressure and combined with the incoming gaseous mixture. The concentration of heavy impurities in the vapor phase is reduced to a sufficient extent such that a product stream concentrated in the lower volatility component will have a reduction in its heavy impurity concentration. The product stream is pumped to pressure and vaporized against a portion of mixture using a boosted pressure subsidiary stream made up of a minor portion of the gaseous mixture.

Cryogenic rectification method and apparatus

The present invention provides an apparatus and method for producing ultra-high purity nitrogen. In accordance with the method and apparatus, air is rectified to produce a tower overhead comprising high purity nitrogen rich in light elements, such as neon, helium and hydrogen. The tower overhead is then partially condensed within a condenser and separated into liquid and vapor phases within a phase separator. The liquid phase is lean in the light elements and the vapor phase is rich in the light elements. The liquid phase is removed from the bottom of the phase separator and is introduced into the column as reflux. As the reflux drops from tray to tray it is stripped of the light elements. A product stream containing ultra-high purity nitrogen is withdrawn as a liquid from the column after suitable stripping of the reflux. The product stream can be further purified by stripping the product stream within a stripper column.

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Highland Park, NJ, United States of America

Sidney S Stern