Process to produce a krypton-xenon concentrate and a gaseous oxygen product

Claim 2

A process for the production of a krypton-xenon concentrate and the recovery of a gaseous product substantially free of rare gases, comprising: (1) taking from an air separation plant a feed liquid comprising oxygen, krypton and xenon wherein the oxygen in the feed liquid comprises from about 5 to 40 percent of the oxygen from the air separation plant and providing said feed liquid to a reboiling zone to form a reboiling liquid; (2) partially vaporizing the reboiling liquid to produce a vapor, and a liquid krypton-xenon concentrate; (3) recovering krypton-xenon concentrate; (4) introducing into a stripping column, reflux liquid having a krypton-xenon concentration less than that in said vapor; (5) passing said vapor against the reflux liquid downflowing in the stripping column; (6) stripping krypton and xenon from the vapor into the reflux liquid to produce a lean vapor and a richer liquid; (7) passing the richer liquid to the reboiling zone to form part of the reboiling liquid; (8) withdrawing lean vapor from the stripping column; (9) recovering withdrawn lean vapor as gaseous product substantially free of rare gases; and (10) recovering the major portion of the oxygen as oxygen gas product directly from the air separation plant, thereby enabling the employment of a stripping column of considerably smaller size then is required for conventional krypton-xenon concentration processes.

Claim 3

The process of claim 1 wherein the krypton concentration in the liquid feed is at least 10 ppm.

Claim 4

The process of claim 1 wherein the richer liquid from the stripping column is combined with feed liquid prior to passage to the reboiling zone.

Claim 5

The process of claim 1 wherein the stripping column operates at a pressure in the range of from 15 to 100 psia.

Claim 6

The process of claim 1 wherein the concentration of krypton in the krypton-xenon concentrate is at least 200 ppm.

Claim 7

The process of claim 1 wherein the feed liquid is taken from the area of heat exchange relation of a double column air separation process.

Claim 8

The process of claim 6 wherein the reflux liquid for the stripping column is provided from the lower pressure column of the double column process and is taken from a point above the point from where the feed liquid is taken.

Claim 9

The process of claim 7 wherein said reflux liquid is taken from the lower pressure column at least two equilibrium stages above the area of heat exchange relation.

Claim 10

The process of claim 6 wherein a gaseous stream is removed from the lower pressure column and recovered as product oxygen.

Claim 11

The process of claim 9 wherein the lean vapor is combined with said gaseous stream and the combined stream is recovered.

Claim 12

The process of claim 9 wherein the gaseous stream is removed from the lower pressure column at a point between the points from where the feed liquid and the reflux liquid are respectively taken.

Claim 13

The process of claim 6 wherein the partial vaporization of the reboiling liquid is carried out by indirect heat exchange with condensing nitrogen-rich vapor taken from the higher pressure column.

Claim 14

The process of claim 12 wherein the resulting condensed nitrogen-rich stream is returned to the higher pressure column as liquid reflux.

Claim 15

A process for the production of a krypton-xenon concentrate and the recovery of gaseous product substantially free of rare gases, comprising: (1) providing feed air to a cryogenic rectification air separation plant comprising a higher pressure column and a lower pressure column in heat exchange relation; (2) withdrawing a first liquid comprising oxygen, krypton and xenon from the area of heat exchange relation and providing said withdrawn liquid to a reboiling zone to form a reboiling liquid; (3) partially vaporizing the reboiling liquid to produce a vapor, and a liquid krypton-xenon concentrate; (4) recovering krypton-xenon concentrate; (5) withdrawing a second liquid from the lower pressure column at a point above the point where the first liquid is withdrawn, said second liquid having a krypton-xenon concentration less than that in the vapor produced in the reboiling zone, and introducing said second liquid into a stripping column as reflux liquid; (6) passing said vapor against the reflux liquid downflowing in the stripping column; (7) stripping krypton and xenon from the vapor into the reflux liquid to produce a lean vapor and a richer liquid; (8) passing the richer liquid to the reboiling zone to form part of the reboiling liquid; (9) withdrawing lean vapor from the stripping column; (10) recovering withdrawn lean vapor as gaseous product substantially free of rare gases; (11) withdrawing from the lower pressure column, at a point between the points from where the first and second liquids are withdrawn, a gaseous stream; and (12) recovering said gaseous stream as product oxygen.

Claim 16

A process for the production of a krypton-xenon concentrate and the recovery of gaseous product substantially free of rare gases, comprising: (1) providing feed air to a cryogenic rectification air separation plant comprising a higher pressure column and a lower pressure column in heat exchange relation; (2) withdrawing a first liquid comprising oxygen, krypton and xenon from the area of heat exchange relation and providing said withdrawn liquid to a reboiling zone to form a reboiling liquid; (3) partially vaporizing the reboiling liquid to produce a vapor, and a liquid krypton-xenon concentrate; (4) recovering krypton-xenon concentrate; (5) withdrawing a second liquid from the lower pressure column at a point above the point where the first liquid is withdrawn, said second liquid having a krypton-xenon concentration less than that in the vapor produced in the reboiling zone, and introducing said second liquid into a stripping column as reflux liquid; (6) passing said vapor against the reflux liquid downflowing in the stripping column; (7) stripping krypton and xenon from the vapor into the reflux liquid to produce a lean vapor and a richer liquid; (8) passing the richer liquid to the reboiling zone to form part of the reboiling liquid; (9) withdrawing lean vapor from the stripping column; (10) recovering withdrawn lean vapor as gaseous product substantially free of rare gases; (11) withdrawing from the lower pressure column, at a point between the points from where the first and second liquids are withdrawn, a gaseous stream; and (12) recovering said gaseous stream as product oxygen.

Claim 17

The process of claim 14 wherein the withdrawn lean vapor and the withdrawn gaseous stream are combined and recovered together.

Claim 18

The process of claim 14 wherein the second liquid is withdrawn from the lower pressure column at least two equilibrium stages above the area of heat exchange relation.

Claim 19

The process of claim 14 wherein the partial vaporization of the reboiling liquid is carried out by indirect heat exchange with condensing nitrogen-rich vapor taken from the higher pressure column.

Claim 20

The process of claim 17 wherein the resulting condensed nitrogen-rich stream is returned to the higher pressure column as liquid reflux.