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US 12,455,114 B2Granted
Systems and methods for removing nitrogen during liquefaction of natural gas
AssigneeConocoPhillips Company
InventorsWill T. James, Matthew C. Gentry, Wesley R. Qualls
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Abstract
Implementations described and claimed herein provide systems and methods for removing nitrogen during liquefaction of natural gas. In one implementation, a nitrogen rejection unit is used in an LNG facility to remove nitrogen from natural gas during an LNG liquefaction process. The nitrogen rejection unit contains at least two columns and at least one 3-stream condenser, 2-stream condenser or a two 2-stream condenser.
Claims19
A method for removing nitrogen from a natural gas stream in a liquefied natural gas facility, the method comprising:
- liquefying the natural gas stream at least partially in the liquefied natural gas facility to form a liquefied natural gas stream;
- routing the liquefied natural gas stream through a nitrogen rejection unit, the nitrogen rejection unit including an upstream nitrogen removal column, a downstream nitrogen removal column, an intermediate nitrogen removal column, a first condenser, and a second condenser;
- condensing a nitrogen-containing stream of the liquefied natural gas stream at least partially via indirect heat exchange using the first condenser and the second condenser, each of the first condenser and the second condenser being independently a 3-stream condenser or a 2-stream condenser, the nitrogen rejection unit removing nitrogen from the liquefied natural gas stream;
- routing the liquefied natural gas stream to the upstream nitrogen removal column, where a first top stream and a first bottom stream form;
- routing a first portion of the first top stream to the first condenser;
- removing a second portion of the first top stream from the nitrogen rejection unit;
- routing a third portion of the first top stream to the intermediate nitrogen removal column;
- removing the first bottom stream from the nitrogen rejection unit, the first bottom stream removed from the nitrogen rejection unit containing heavies;
- routing the first portion of the first top stream from the first condenser to the intermediate nitrogen removal column, where a second top stream and a second bottom stream are formed;
- routing at least a portion of the second top stream to the second condenser before routing to the downstream nitrogen removal column;
- forming a third top stream and a third bottom stream in the downstream nitrogen removal column, wherein the third top stream comprises predominantly nitrogen;
- routing the third bottom stream to an expansion drum;
- forming a liquid stream and a gas stream using the expansion drum;
- routing the liquid stream to the first condenser, the first condenser warming the liquid stream to form a warmed liquid stream before exiting the nitrogen rejection unit;
- and
- combining the gas stream with the warmed liquid stream.
13 more elements
A liquefied natural gas system comprising:
- one or more refrigeration cycles successively cooling a fluid stream, each of the one or more refrigeration cycles including a refrigerant, a compressor, and a chiller;
- an upstream nitrogen removal column of a nitrogen rejection unit wherein the upstream nitrogen removal column is operable to form a first top stream and a first bottom stream from a nitrogen-containing stream, the first bottom stream removed from the nitrogen rejection unit, and the first bottom stream removed from the nitrogen rejection unit containing heavies;
- a downstream nitrogen removal column of the nitrogen rejection unit;
- an intermediate nitrogen removal column of the nitrogen rejection unit disposed between the upstream nitrogen removal column and the downstream nitrogen removal column;
- a first condenser of the nitrogen rejection unit, wherein a first portion of the first top stream is routed to the first condenser before being routed to the intermediate nitrogen removal column, a second portion of the first top stream is removed from the nitrogen rejection unit, and a third portion of the first top stream is routed to the intermediate nitrogen removal column, and wherein the intermediate nitrogen removal column is operable to form a second top stream and a second bottom stream;
- a second condenser of the nitrogen rejection unit, wherein at least a portion of the second top stream is routed to the second condenser before routing to the downstream nitrogen removal column, and wherein the first condenser and second condenser at least partially condense the nitrogen-containing stream via indirect heat exchange, and each of the first condenser and the second condenser are independently a 3-stream condenser, or a 2-stream condenser;
- and
- an expansion drum of the nitrogen rejection unit configured to receive a third bottom stream formed in the downstream nitrogen removal column, the expansion drum configured to form a liquid stream and a gas stream, the liquid stream routed to the first condenser, the first condenser warming the liquid stream before exiting the nitrogen rejection unit to form a warmed liquid stream, the gas stream combined with the warmed liquid stream.
5 more elements
Dependencies are inferred from the claim text.