Dephlegmator process for the recovery of helium

Claim 2

In a process for separating a crude helium product having a helium concentration greater than thirty percent by volume from a pressurized, helium-containing feed gas mixture, wherein the pressurized, helium-containing feed gas mixture is separated to produce a helium-enriched stream and a helium-lean stream, and wherein the helium-enriched stream is further upgraded to produce the crude helium product and at least one residue gas product stream, the improvement for more effectively upgrading the helium-enriched stream to produce the crude helium product comprises the steps of: (a) rectifying the helium-enriched stream in a dephlegmator heat exchanger thereby producing a helium-rich overhead stream and a dephlegmator helium-lean liquid stream; (b) removing the helium-rich overhead stream from the dephlegmator heat exchanger as the crude helium product and warming the crude helium product to recover refrigeration for the dephlegmator heat exchanger; (c) expanding and warming the helium-lean liquid stream to recover refrigeration for the dephlegmator heat exchanger thereby producing a residue stream; and (d) further warming the residue stream and the crude helium product to recover refrigeration for the liquefaction of the pressurized, helium-containing feed gas mixture.

Claim 3

The process of claim 1 which further comprises cooling and partially condensing the helium-enriched stream and phase separating out the produced liquids prior to rectification in step (a) and combining the produced liquids with the dephlegmator helium-lean liquid stream prior to expanding the dephlegmator liquid stream in step (c).

Claim 4

The process of claim 1 wherein in expanding and warming the dephlegmator helium-lean liquid stream to recover refrigeration of step (c) comprises dividing the helium-lean liquid stream into two portions; expanding the first portion to produce a lower pressure residue stream and warming the lower pressure residue stream to recover refrigeration for the dephlegmator heat exchanger.

Claim 5

The process of claim 1 wherein the helium-containing feed gas mixture comprises helium, natural gas and nitrogen.

Claim 6

In a process for separating a crude helium product having a helium concentration greater than thirty percent by volume from a pressurized, helium-containing feed gas mixture, wherein the pressurized, helium-containing feed gas mixture is separated to produce a helium-enriched stream and a helium-lean stream, and wherein the helium-enriched stream is further upgraded to produce the crude helium product and at least one residue gas product stream, the improvement for more effectively upgrading the, helium-enriched stream to produce the crude helium product comprises the steps of: (a) rectifying the helium-rich vapor stream in a dephlegmator heat exchanger thereby producing a helium-rich overhead stream and a dephlegmator helium-lean liquid stream; (b) removing the helium-rich overhead stream from the dephlegmator heat exchanger as the crude helium product and warming the crude helium product to recover refrigeration for the dephlegmator heat exchanger; (c) flashing the dephlegmator helium-lean liquid stream thereby producing a partially vaporized helium-lean stream; (d) phase separating the partially vaporized helium-lean stream thereby producing a nitrogen-rich vapor stream and a first nitrogen-lean liquid; (e) rectifying the nitrogen-rich vapor stream in the dephlegmator heat exchanger thereby producing a nitrogen-rich overhead stream and a second nitrogen-lean liquid; (f) removing the helium-rich overhead stream from the dephlegmator and warming it to recover refrigeration for the dephlegmator heat exchanger; (g) combining the first and second nitrogen-lean liquids and cooling the combined nitrogen-lean liquids stream; (h) expanding and warming the combined nitrogen-lean liquids stream to recover refrigeration for the dephlegmator heat exchanger thereby producing a residue stream; and (i) further warming the residue stream and the crude helium product to recover refrigeration for the liquefaction of the pressurized, helium-containing feed gas mixture.

Claim 7

In a process for separating a crude helium product having a helium concentration greater than thirty percent by volume from a pressurized, helium-containing feed gas mixture, wherein the pressurized, helium-containing feed gas mixture is separated to produce a helium-enriched stream and a helium-lean stream, and wherein the helium-enriched stream is further upgraded to produce the crude helium product and at least one residue gas product stream, the improvement for more effectively upgrading the, helium-enriched stream to produce the crude helium product comprises the steps of: (a) rectifying the helium-rich vapor stream in a dephlegmator heat exchanger thereby producing a helium-rich overhead stream and a dephlegmator helium-lean liquid stream; (b) removing the helium-rich overhead stream from the dephlegmator heat exchanger as the crude helium product and warming the crude helium product to recover refrigeration for the dephlegmator heat exchanger; (c) flashing the dephlegmator helium-lean liquid stream thereby producing a partially vaporized helium-lean stream; (d) phase separating the partially vaporized helium-lean stream thereby producing a nitrogen-rich vapor stream and a first nitrogen-lean liquid; (e) rectifying the nitrogen-rich vapor stream in the dephlegmator heat exchanger thereby producing a nitrogen-rich overhead stream and a second nitrogen-lean liquid; (f) removing the helium-rich overhead stream from the dephlegmator and warming it to recover refrigeration for the dephlegmator heat exchanger; (g) combining the first and second nitrogen-lean liquids and cooling the combined nitrogen-lean liquids stream; (h) expanding and warming the combined nitrogen-lean liquids stream to recover refrigeration for the dephlegmator heat exchanger thereby producing a residue stream; and (i) further warming the residue stream and the crude helium product to recover refrigeration for the liquefaction of the pressurized, helium-containing feed gas mixture.

Claim 8

The process of claim 5 which further comprises cooling and partially condensing the helium-enriched stream and phase separating out the produced liquids prior to rectification in step (a) and combining the produced liquids to the dephlegmator liquid stream prior to flashing of the dephlegmator liquid in step (c).

Claim 9

The process of claim 5 wherein in expanding and warming the combined nitrogen-lean liquids stream to recover refrigeration of step (h) comprises dividing the nitrogen-lean liquids stream into two portions; expanding the first portion to produce a lower pressure residue stream and warming the lower pressure residue stream to recover refrigeration for the dephlegmator; expanding the second portion to produce a higher pressure residue stream and warming the higher pressure residue stream to recover refrigeration for the dephlegmator.

Claim 10

The process of claim 5 wherein the helium-containing feed gas mixture comprises helium, natural gas and nitrogen.

Claim 11

A process for separating a crude helium product stream having a helium concentration greater than thirty percent by volume from a pressurized, helium-containing feed gas mixture comprising the steps of: (a) liquefying and subcooling the pressurized, helium-containing feed gas mixture; (b) expanding the liquefied, subcooled, pressurized, helium-containing feed gas mixture whereby said liquefied mixture is partially vaporized and thereby producing a partially vaporized fractionation feed stream; (c) stripping the partially vaporized fractionation feed stream in a cryogenic distillation column thereby producing as an overhead, the helium-enriched stream, and a bottoms liquid, the helium-lea stream; (d) reboiling the cryogenic distillation column by vaporizing at least a portion of the helium-lean stream; (e) rectifying the helium-enriched stream in a dephlegmator heat exchanger thereby producing a helium-rich overhead stream and a dephlegmator helium-lean liquid stream; (f) removing the helium-rich overhead stream from the dephlegmator heat exchanger as the crude helium product and warming the crude helium product to recover refrigeration for the dephlegmator heat exchanger; (g) expanding and warming the helium-lean liquid stream to recover refrigeration for the dephlegmator heat exchanger thereby producing a residue stream; and (d) further warming the residue stream and the crude helium product to recover refrigeration for the liquefaction of the pressurized, helium-containing feed gas mixture.

Claim 12

A process for separating a crude helium product stream having a helium concentration greater than thirty percent by volume from a pressurized, helium-containing feed gas mixture comprising the steps of: (a) liquefying and subcooling the pressurized, helium-containing feed gas mixture; (b) expanding the liquefied, subcooled, pressurized, helium-containing feed gas mixture whereby said liquefied mixture is partially vaporized and thereby producing a partially vaporized fractionation feed stream; (c) stripping the partially vaporized fractionation feed stream in a cryogenic distillation column thereby producing as an overhead, the helium-enriched stream, and a bottoms liquid, the helium-lea stream; (d) reboiling the cryogenic distillation column by vaporizing at least a portion of the helium-lean stream; (e) rectifying the helium-enriched stream in a dephlegmator heat exchanger thereby producing a helium-rich overhead stream and a dephlegmator helium-lean liquid stream; (f) removing the helium-rich overhead stream from the dephlegmator heat exchanger as the crude helium product and warming the crude helium product to recover refrigeration for the dephlegmator heat exchanger; (g) expanding and warming the helium-lean liquid stream to recover refrigeration for the dephlegmator heat exchanger thereby producing a residue stream; and (d) further warming the residue stream and the crude helium product to recover refrigeration for the liquefaction of the pressurized, helium-containing feed gas mixture.

Claim 13

The process of claim 9 wherein in expanding and warming the dephlegmator helium-lean liquid stream to recover refrigeration of step (g) comprises dividing the helium-lean liquid stream into two portions; expanding the first portion to produce a lower pressure residue stream and warming the lower pressure residue stream to recover refrigeration for the dephlegmator heat exchanger; expanding the second portion to produce a higher pressure residue stream and warming the higher pressure residue stream to recover refrigeration for the dephlegmator heat exchanger.

Claim 14

The process of claim 9 wherein the liquefied, subcooled pressurized, helium-containing feed gas mixture is expanded so as to produce mechanical work.

Claim 15

The process of claim 9 wherein the liquefied, subcooled pressurized, helium-containing feed gas mixture is expanded across a hydraulic turbine.

Claim 16

The process of claim 9 which further comprises cooling and partially condensing the helium-enriched stream and phase separating out the produced liquids prior to rectification in step (e) and combining the produced liquids to the dephlegmator liquid stream prior to dividing the dephlegmator liquid stream in step (g).

Claim 17

The process of claim 9 wherein the helium-containing feed gas mixture comprises helium, natural gas and nitrogen.

Claim 18

A process for separating a crude helium product stream having a helium concentration greater than thirty percent by volume from a pressurized, helium and nitrogen containing feed gas mixture comprising the steps of: (a) liquefying and subcooling the pressurized, feed gas mixture; (b) expanding the liquefied, subcooled, pressurized, feed gas mixture whereby said liquefied mixture is partially vaporized and thereby producing a partially vaporized fractionation feed stream; (c) stripping the partially vaporized fractionation feed stream in a cryogenic distillation column thereby producing as an overhead, the helium-enriched stream, and a bottoms liquid, the helium-lean stream; (d) reboiling the cryogenic distillation column by vaporizing at least a portion of the helium-lean stream; (e) rectifying the helium-rich vapor stream in the dephlegmator heat exchanger thereby producing a helium-rich overhead stream and a dephlegmator helium-lean liquid stream; (f) removing the helium-rich overhead stream from the dephlegmator heat exchanger as the crude helium product and warming the crude helium product to recover refrigeration for the dephlegmator heat exchanger; (g) flashing the dephlegmator helium-lean liquid stream thereby producing a partially vaporized helium-lean stream; (h) phase separating the partially vaporized helium-lean stream thereby producing a nitrogen-rich vapor stream and a first nitrogen-lean liquid; (i) rectifying the nitrogen-rich vapor stream in a dephlegmator heat exchanger thereby producing a nitrogen-rich overhead stream and a second nitrogen-lean liquid; (j) removing the helium-rich overhead stream from the dephlegmator heat exchanger and warming it to recover refrigeration for the dephlegmator heat exchanger; (k) combining the first and second nitrogen-lean liquids and cooling the combined nitrogen-lean liquids stream; (1) expanding and warming the combined nitrogen-lean liquids stream to recover refrigeration for the dephlegmator heat exchanger thereby producing a residue stream; and (m) further warming the residue stream and the crude helium product to recover refrigeration for the liquefaction of the pressurized, helium-containing feed gas mixture.

Claim 19

A process for separating a crude helium product stream having a helium concentration greater than thirty percent by volume from a pressurized, helium and nitrogen containing feed gas mixture comprising the steps of: (a) liquefying and subcooling the pressurized, feed gas mixture; (b) expanding the liquefied, subcooled, pressurized, feed gas mixture whereby said liquefied mixture is partially vaporized and thereby producing a partially vaporized fractionation feed stream; (c) stripping the partially vaporized fractionation feed stream in a cryogenic distillation column thereby producing as an overhead, the helium-enriched stream, and a bottoms liquid, the helium-lean stream; (d) reboiling the cryogenic distillation column by vaporizing at least a portion of the helium-lean stream; (e) rectifying the helium-rich vapor stream in the dephlegmator heat exchanger thereby producing a helium-rich overhead stream and a dephlegmator helium-lean liquid stream; (f) removing the helium-rich overhead stream from the dephlegmator heat exchanger as the crude helium product and warming the crude helium product to recover refrigeration for the dephlegmator heat exchanger; (g) flashing the dephlegmator helium-lean liquid stream thereby producing a partially vaporized helium-lean stream; (h) phase separating the partially vaporized helium-lean stream thereby producing a nitrogen-rich vapor stream and a first nitrogen-lean liquid; (i) rectifying the nitrogen-rich vapor stream in a dephlegmator heat exchanger thereby producing a nitrogen-rich overhead stream and a second nitrogen-lean liquid; (j) removing the helium-rich overhead stream from the dephlegmator heat exchanger and warming it to recover refrigeration for the dephlegmator heat exchanger; (k) combining the first and second nitrogen-lean liquids and cooling the combined nitrogen-lean liquids stream; (1) expanding and warming the combined nitrogen-lean liquids stream to recover refrigeration for the dephlegmator heat exchanger thereby producing a residue stream; and (m) further warming the residue stream and the crude helium product to recover refrigeration for the liquefaction of the pressurized, helium-containing feed gas mixture.

Claim 20

The process of claim 15 wherein in expanding and warming the combined nitrogen-lean liquids stream to recover refrigeration of step (l) comprises dividing the nitrogen-lean liquids stream into two portions; expanding the first portion to produce a lower pressure residue stream and warming the lower pressure residue stream to recover refrigeration for the dephlegmator heat exchanger; expanding the second portion to produce a higher pressure residue stream and warming the higher pressure residue stream to recover refrigeration for the dephlegmator heat exchanger.

Claim 21

The process of claim 15 wherein the liquefied, subcooled pressurized, helium-containing feed gas mixture is expanded so as to produce methanical work.

Claim 22

The process of claim 15 wherein the liquefied, subcooled pressurized, helium-containing feed gas mixture is expanded across a hydraulic turbine.

Claim 23

The process of claim 15 which further comprises cooling and partially condensing the helium-enriched stream and phase separating out the produced liquids prior to rectification in step (e) and combining the produced liquids to the dephlegmator liquid stream prior to flashing the dephlegmator stream in step (g).

Claim 24

The process of claim 15 wherein the helium-containing feed gas mixture comprises helium, natural gas and nitrogen.

Claim 25

A dephlegmator heat exchanger process for the separation of a light gas from a gas mixture comprising at least the light gas and a heavier gas comprising the following steps: (a) rectifying the gas mixture in a dephlegmator heat exchanger thereby producing a light gas-rich overhead stream and a light gas-lean liquid stream; (b) removing the light gas-rich overhead stream from the dephlegmator heat exchanger as the crude light gas product and warming the crude light gas product to recover refrigeration for the dephlegmator heat exchanger; and (c) expanding and warming the light gas-lean liquid stream to recover refrigeration for the dephlegmator heat exchanger.

Claim 26

A dephlegmator heat exchanger process for the separation of a light gas from a gas mixture comprising at least the light gas and a heavier gas comprising the following steps: (a) rectifying the gas mixture in a dephlegmator heat exchanger thereby producing a light gas-rich overhead stream and a light gas-lean liquid stream; (b) removing the light gas-rich overhead stream from the dephlegmator heat exchanger as the crude light gas product and warming the crude light gas product to recover refrigeration for the dephlegmator heat exchanger; and (c) expanding and warming the light gas-lean liquid stream to recover refrigeration for the dephlegmator heat exchanger.