초록 ▼

A compressed gas mixture, for example air, is passed through one of beds 12 and 14 of adsorbent that selectively adsorbs oxygen from the air. Unadsorbed nitrogen-enriched gas flows into a buffer vessel 28, from which product gas is withdrawn through pipeline 30. While one of the beds 12 and 14 is ad

A compressed gas mixture, for example air, is passed through one of beds 12 and 14 of adsorbent that selectively adsorbs oxygen from the air. Unadsorbed nitrogen-enriched gas flows into a buffer vessel 28, from which product gas is withdrawn through pipeline 30. While one of the beds 12 and 14 is adsorbing oxygen for air the other is being regenerated, and during this period the communication between the beds is denied. At the end of a chosen period of time the beds are placed in communication with one another by opening valves 54 and 56. Then the bed that was previously being regenerated is placed in communication with the source of compressed air and the other bed regenerated. The period of intercommunication between the beds lasts for as long as it takes the volume of product gas as measured by an integrating flow meter 31 from the start of the preceding adsorption step to reach a chosen value. The apparatus is able to supply nitrogen of a chosen purity at a variable flow rate.

대표청구항 ▼

An improved process for the separation of a gas mixture comprising the steps of: (a) repeatedly performing a cycle of operations employing a first vessel containing adsorbent which adsorbs one component of the gas mixture more readily then another or the other component of the gas mixture, the cycle

An improved process for the separation of a gas mixture comprising the steps of: (a) repeatedly performing a cycle of operations employing a first vessel containing adsorbent which adsorbs one component of the gas mixture more readily then another or the other component of the gas mixture, the cycle of operations comprising: (i) passing the gaseous mixture at super-atmospheric pressure through the vessel whereby said one component is adsorbed and a gas stream relatively lean in the adsorbed component flows out of the bed, this adsorption step of the cycle of operations lasting a chosen constant period of time; (ii) regenerating the adsorbent by desorbing gas therefrom and causing a gas stream relatively rich in the desorbed gas to flow out of the vessel; (b) repeatedly performing such a cycle of operations employing a second vessel containing said adsorbent, the cycles being phased relative to one another, such that at no time is step (i) or step (ii) in one cycle performed simultaneously with the corresponding steps in the other cycle; and (c) passing the gas stream relatively lean in the adsorbed component into a reservoir; the improvement which comprises continously withdrawing the gas from the reservoir, measuring the flow of gas from the reservoir, and controlling the commencement of the adsorption step in one cycle, such that said adsorption step starts after completion of a preceding adsorption step in the other cycle but only upon the volume of gas withdrawn from the reservoir, measured from the commencement of the preceding adsorption step, having reached a predetemined value. An improved process for the separation of air, comprising the steps of: (a) repeatedly performing a cycle of operation employing a first vessel containing molecular sieve coke which adsorbs oxygen, carbon dioxide and water vapour more readily than nitrogen, the cycle of operations comprising; (i) passing air at super-atmospheric pressure through the vessel whereby oxygen, carbon dioxide and water vapour are adsorbed and a gas stream relatively rich in nitrogen flows out of the bed, this adsorption step of the cycle of operations lasting a chosen constant period of time; (ii) regenerating the molecular sieve coke by desorbing oxygen, carbon dioxide and water vapour therefrom and causing a gas stream relatively rich in said oxygen, carbon dioxide and water vapour to flow out of the vessel; (b) repeatedly performing such a cycle of operations employing a second vessel containing molecular sieve coke, the cycles being phased relative to one another, such that at no time is step (i) or step (ii) in one cycle performed simultaneously with the corresponding step in the other cycle; and (c) passing the nitrogen into at least one reservoir; the impovement comprising continuously withdrawing the nitrogen from the reservoir and measuring its flow rate by means of an integrating flowmeter, controlling the commencement of th adsorption step in one cycle, such that said adsorption step starts after a preceding adsorption step in the other cycle is completed but only upon the nitrogn withdrawn from the reservoir, measured from the commencement of the preceding adsorption step, having reached a predetermined value.