INTEGRATED NITROGEN REJECTION FOR LIQUEFACTION OF NATURAL GAS
A method and system for controlling the nitrogen concentration in an LNG product and fuel from flash gas within preferred ranges. A cooled LNG stream is separated into a nitrogen-enriched vapor stream, a fuel stream, and an LNG product stream using a plurality of phase separating devices, such as flash drum or rectifying column. A portion of the vapor stream is recycled to the rectifying column as reflux. A portion of a stream having a higher concentration of nitrogen is combined with the fuel stream to maintain the fuel stream within a desired nitrogen concentration range.
1 . A method for liquefying a natural gas feed stream and removing nitrogen therefrom, the method comprising:
(a) cooling and at least partially liquefying a natural gas feed stream to form a cooled LNG stream having a cooled LNG nitrogen concentration;
(b) performing a plurality of phase separations in downstream fluid flow communication with the cooled LNG stream to produce a nitrogen vapor stream having a vapor stream nitrogen concentration, a fuel stream having a fuel stream nitrogen concentration, and an LNG product stream having an LNG product stream nitrogen concentration, wherein the vapor stream nitrogen concentration is greater than the cooled LNG nitrogen concentration, the fuel stream nitrogen concentration and the LNG product stream nitrogen concentration,
(c) combining the fuel stream with a mixing stream to create a fuel product stream having a fuel product stream nitrogen concentration, the fuel product stream nitrogen concentration being greater than the fuel stream nitrogen concentration, the mixing stream being in downstream fluid flow communication with the cooled LNG stream; and
(d) recycling a recycle stream comprising a portion of the nitrogen vapor stream as reflux for a rectification column;
whereby step (c) enables the fuel product stream nitrogen concentration to be controlled independently of the LNG product stream nitrogen concentration.
2 . The method of claim 1 , wherein step (c) further comprises controlling flow of the mixing stream to produce a fuel product stream nitrogen concentration that is within a predetermined fuel product stream nitrogen concentration range.
3 . The method of claim 1 , wherein at least one of the plurality of phase separations of step (b) is performed in a rectification column and the fuel stream is withdrawn as a liquid from a bottom end of the rectification column.
4 . The method of claim 1 , further comprising:
(e) cooling the recycle stream against the nitrogen vapor stream and the fuel stream.
5 . The method of claim 4 , wherein step (e) further comprises vaporizing the fuel stream to cool the recycle stream.
6 . The method of claim 4 , further comprising:
(d1) compressing and performing an ambient heat exchange on the recycle stream before performing step (e).
7 . The method of claim 1 , further comprising:
(f) powering at least one gas turbine using the fuel product stream.
8 . The method of claim 7 , further comprising:
(g) driving at least one compressor adapted to compress a refrigerant used to perform step (a) using the fuel product stream.
9 . The method of claim 1 , wherein the plurality of phase separations further comprises phase separating the cooled LNG stream to produce a flash gas stream and the LNG product stream.
10 . The method of claim 9 , wherein the cooled LNG stream is phase separated using a flash drum.
11 . The method of claim 9 , wherein the cooled LNG stream is phase separated using a rectification column.
12 . The method of claim 9 , wherein the plurality of phase separations further comprises introducing at least a first portion of the flash gas stream into the rectification column to produce the nitrogen vapor stream and the fuel stream.
13 . The method of claim 12 , wherein the mixing stream comprises a second portion of the flash gas stream.
14 . The method of claim 1 , wherein the mixing stream is combined with the fuel stream downstream from step (e).
15 . The method of claim 1 , wherein the mixing stream is compressed and cooled before being combined with the fuel stream.
16 . The method of claim 1 , further comprising:
(h) venting the nitrogen vapor stream.
17 . The method of claim 1 , further comprising:
(h) storing the nitrogen vapor stream.
18 . The method of claim 1 , wherein step (d) further comprises controlling flow of the mixing stream to produce a fuel product stream nitrogen concentration that is within a predetermined fuel product stream nitrogen concentration range.
19 . A method for liquefying a natural gas feed stream and removing nitrogen therefrom, the method comprising:
(a) at least partially liquefying a natural gas feed stream in a main cryogenic heat exchanger to form a cooled LNG stream having a cooled LNG nitrogen concentration;
(b) separating the cooled LNG stream into an LNG product stream having an LNG product stream nitrogen concentration and a flash gas stream having a flash gas stream nitrogen concentration in a flash drum or rectification column;
(c) separating at least a first portion of the flash gas stream in a rectification column to produce a nitrogen vapor stream having a vapor stream nitrogen concentration, and a fuel stream having a fuel stream nitrogen concentration;
(d) combining the fuel stream with a mixing stream to form a fuel product stream having a fuel product stream nitrogen concentration that is higher than the fuel stream nitrogen concentration, the mixing stream comprising a second portion of the flash gas stream;
(e) dividing the nitrogen vapor stream into a recycle stream and a vent stream;
(f) compressing and cooling the recycle stream; and
(g) further cooling the recycle stream by indirect heat exchange against the fuel stream and the nitrogen vapor stream.
20 . The method of claim 19 , wherein the vapor stream nitrogen concentration is greater than the cooled LNG nitrogen concentration, the fuel stream nitrogen concentration, and the LNG product stream nitrogen concentration.
21 . The method of claim 19 , wherein step (d) enables the fuel product stream nitrogen concentration to be controlled independently of the LNG product stream nitrogen concentration.