초록 ▼

A method is provided for the extraction of hellium of high purity, and high yield, with intermediate enrichment in refrigerating plants, from gases containing very low helium concentrations, by an alternating pressure adsorption process. the helium containing gas is fed cyclically in each of three a

A method is provided for the extraction of hellium of high purity, and high yield, with intermediate enrichment in refrigerating plants, from gases containing very low helium concentrations, by an alternating pressure adsorption process. the helium containing gas is fed cyclically in each of three adsorption stages into four adsorbers connected in parallel. First, higher hydrocarbons and other impurities are trapped in adsorbers (J, K, L, M) filled with activated charcoal in a preliminary filtering stage. Other gaseous components, for example nitrogen and/or methane are trapped in adsorbers (A, B, C, D and E, F, G, H) filled with carbon molecular sieves, in two subsequent adsorption stages. The helium is first enriched in stage (I) and then extracted in stage (II) as refined helium with a helium content of 99.9%. The gas used is preferably natural gas with a 2 to 10% helium content. The refined helium so produced can be used, for example as a blanket gas, a breathing gas for divers, a balloon gas and as a carrier gas in chromatography.

대표청구항 ▼

A method for helium recovery according to a pressure swing adsorption process from a gas mixture comprising helium, nitrogen and methane, said method comprising: (a) directing said gas mixture through a plurality of prefiltering adsorbers filled with activated carbon thereby removing higher molecula

A method for helium recovery according to a pressure swing adsorption process from a gas mixture comprising helium, nitrogen and methane, said method comprising: (a) directing said gas mixture through a plurality of prefiltering adsorbers filled with activated carbon thereby removing higher molecular weight hydrocarbons and other contaminants to provide a helium enriched gas composition; (b) conveying said enriched gas composition from said prefiltering adsorbers to a plurality of respective stage I adsorbers arranged in parallel; (c) cyclically feeding said enriched gas composition through said plurality of stage I adsorbers to accomplish a first adsorption stage, said adsorbers being filled with carbon molecular sieves with an average adsorption pore diameter ranging between 0.1 and 0.4 nm for removing nitrogen and methane, said first adsorption stage comprising a multistep pressure build-up phase and a multistep pressure relief phase after adsorption, wherein: (c, a) said pressure build-up phase comprises: 1. a pressure build-up step from a final vacuum pressure (P1) to a medium pressure level (P3); 2. a pressure build-up step from said medium pressure level (P3) to a higher pressure level (P4); 3. a pressure build-up step from said higher pressure level (P4) to a highest pressure level (P5); (c, b) said pressure relief phase comprises: 1. a pressure relief step from said highest pressure level (P5) down to said higher pressure level (P4); 2. a pressure relief step from said higher pressure level (P4) to said medium pressure level (P3); 3. a pressure relief step from said medium pressure level (P3) to an ambient pressure (P2); 4. a pressure relief step from said ambient pressure level (P2) to said final vacuum pressure (P1); (c, c) pressure compensation taking place in a first compensation step occurring between an outlet of a first of said stage I adsorbers which performs said pressure relief step (1) from P5 down to P4 and between an outlet of a second of said stage I adsorbers performing said pressure build-up step (2) from P3 to P4, and a second compensation step occurring between an outlet of said first adsorber which performs said pressure relief step (2) from P4 down to P3 and said inlet of a third stage I adsorber performing said pressure build-up step (1) from P to P3; and (c, d) said pressure relief steps (3) and (4) occurring in counterflow whereby a helium-poor waste gas results and said pressure build-up step (3) is performed with a product gas; (d) cyclically feeding said product gas coming from said first adsorption stage to a plurality of stage II adsorbers arranged in parallel, said stage II adsorbers also being filled with said carbon molecular sieves, said product gas being successively alternately subjected in each stage II adsorber to a pressure build-up, an adsorption and a regeneration phase, said pressure build-up phase being performed through pressure compensation with molecular sieve material to be regenerated and then with pressure from said product gas, and said regeneration phase beginning with pressure compensation followed by pressure relief and flushing with said product gas, and upon completion of traverse through said stage II adsorbers there results a waste gas which is recycled for further treatment in said first adsorption stage.