Process to separate nitrogen from natural gas

Claim 2

In a process for removing nitrogen from natural gases wherein a nitrogen-containing hydrocarbon stream is first separated into a liquid, containing primarily hydrocarbons having two or more carbon atoms, and into a vapor containing primarily nitrogen and methane, and wherein the vapor stream is further separated in one or more rectification columns into nitrogen and methane, the improvement comprising recovering substantially all of the hydrocarbons containing two or more carbon atoms which were present in the nitrogen-containing hydrocarbon stream by the steps of: (a) cooling the vapor after the first separation by at least 10° K. to partially condense it; (b) introducing the condensed portion into a stripping column where it is separated into a liquid, containing primarily hydrocarbons having two or more carbon atoms, and into a vapor containing primarily methane; (c) recovering the hydrocarbon liquid and the methane vapor of step (B); and (d) introducing the uncondensed portion into the rectification column(s) to be separated into nitrogen and methane.

Claim 3

The process of claim 1 wherein the vapor after the first separation is cooled by at least 20° K.

Claim 4

The process of claim 1 wherein the vapor after the first separation is cooled by ay least 30° K.

Claim 5

The process of claim 1 wherein the stripping column is operated at a pressure at least 50 psi lower than the pressure of the vapor from the first separation.

Claim 6

The process of claim 1 wherein said cooling of step (A) is accomplished at least in part by indirect heat exchange of the vapor after the first separation with the methane vapor from the stripping column.

Claim 7

The process of claim 1 comprising maintaining said rectification column(s) at lower than conventional pressures, but precluding vacuum conditions in a heat pump circuit by the steps of: (a) introducing said uncondensed portion as a nitrogen-containing natural gas feed into a rectification column operating at a pressure in the range of from 200 to 450 psia; (b) separating the feed in said column into a nitrogen-rich top vapor and a methane-rich bottom liquid; (c) cooling the top vapor by indirect heat exchange with vaporizing heat pump fluid comprising from 0.5 to 60 mole percent nitrogen and 99.5 to 40 mole percent methane, to partially condense said top vapor; (d) returning the condensed portion of the top vapor to the column as liquid reflux and removing from the process the uncondensed portion of the top vapor as nitrogen; (e) warming the bottom liquid by indirect heat exchange with condensing said heat pump fluid to partially vaporize said bottom liquid; and (f) returning the vaporized portion of the bottom liquid to the column as vapor reflux and recovering the unvaporized portion as product natural gas; wherein said heat pump fluid is at all times at or greater than ambient pressure.

Claim 8

The process of claim 6 wherein said heat pump fluid has a composition of from 1 to 30 mole percent nitrogen and from 99 to 70 mole percent methane.

Claim 9

The process of claim 6 wherein said heat pump fluid has a composition of from 5 to 20 mole percent nitrogen and from 95 to 80 mole percent methane.

Claim 10

The process of claim 6 wherein said heat pump fluid recirculates in a closed loop comprising: (1) cooling the heat pump fluid by indirect heat exchange with the bottom liquid; (2) dividing the cooled heat pump fluid into a first portion and a second portion; (3) expanding the first portion to a pressure at least equal to ambient pressure and warming the expanded first portion by indirect heat exchange with the top vapor; (4) expanding the second portion to an intermediate pressure, greater than the pressure to which the first portion is expanded, and warming the expanded second portion by indirect heat exchange with a vapor stream taken from an intermediate point in the column; and (5) compressing the expanded first and second portions to form the heat pump fluid to be cooled in step (1).

Claim 11

The process of claim 9 wherein in step (4) the intermediate vapor stream is at least partially condensed and is returned to the column as reflux.

Claim 12

The process of claim 9 wherein at least one of the warmed expanded portions are further warmed prior to compression by indirect heat exchange with the heat pump fluid prior to its expansion.

Claim 13

The process of claim 9 wherein the heat pump fluid is additionally cooled prior to its expansion by indirect heat exchange with the uncondensed portion of the top vapor prior to its removal from the process.

Claim 14

The process of claim 9 wherein the first portion is compressed to said intermediate pressure, combined with the second portion, and the combined stream is compressed to form the heat pump fluid to be cooled in step (1).