Nitrogen recovery apparatus and method of recovering nitrogen
Abstract
A nitrogen recovery apparatus for recovering nitrogen from natural gas comprises a separator having a liquid fraction port and a vapour fraction port in fluid communication with a split flow arrangement, the split flow arrangement having a sub-cooled fluid path and an expanded fluid path. A fractionating column has a reflux inlet port in fluid communication with the subcooled fluid path above a middle feed port thereof, the middle feed port being in fluid communication with the expanded fluid path. A bottom feed port of the fractionating column is in fluid communication with the liquid fraction port of the separator. A side reboiler circuit and a reboiler circuit are operably coupled to the fractionating column below the bottom feed port. A bottom hydrocarbon product stream path is in fluid communication with a bottom hydrocarbon port of the fractionating column.
Claims
exact text as granted — not AI-modified1 . A nitrogen recovery apparatus ( 100 ) for recovering nitrogen from natural gas, the apparatus ( 100 ) comprising:
a separator ( 110 ) having a liquid fraction port and a vapour fraction port in fluid communication with a split flow arrangement ( 112 ), the split flow arrangement ( 112 ) having a sub-cooled fluid path ( 118 ) and an expanded fluid path ( 120 ); a fractionating column ( 116 ) having a reflux inlet port ( 124 ) in fluid communication with the subcooled fluid path ( 118 ) above a middle feed port ( 130 ) thereof, the middle feed port ( 130 ) being in fluid communication with the expanded fluid path ( 120 ); a bottom feed port ( 114 ) of the fractionating column ( 116 ) in fluid communication with the liquid fraction port of the separator ( 110 ); a side reboiler circuit ( 132 ) operably coupled to the fractionating column ( 116 ) below the bottom feed port ( 114 ); a reboiler circuit ( 140 ) operably coupled to the fractionating column ( 116 ) below the side boiler circuit ( 132 ); and a bottom hydrocarbon product stream path ( 160 ) in fluid communication with a bottom hydrocarbon port ( 162 ) of the fractionating column ( 116 ).
2 . An apparatus as claimed in claim 1 , wherein the separator ( 110 ) comprises a feed inlet port for receiving partially liquefied natural gas.
3 . An apparatus as claimed in claim 2 , further comprising:
a heat exchanger ( 108 ) having a natural gas feed inlet port, the heat exchanger ( 108 ) also having an output port; wherein the output port is in fluid communication with the feed inlet port of the separator ( 110 ).
4 . An apparatus as claimed in claim 1 , wherein the fractionating column ( 116 ) further comprises:
an overhead gas stream path ( 148 ) arranged to support sub-cooling in the subcooled fluid path ( 118 ).
5 . An apparatus as claimed in claim 4 , wherein the overhead gas stream path ( 148 ) is also in fluid communication with the heat exchanger ( 108 ).
6 . An apparatus as claimed in claim 1 , further comprising:
a reflux condenser stream circuit ( 184 ) which is fed by a drawn off from the fractionating column ( 116 ) from below the middle feed ( 130 ), the reflux condenser stream circuit ( 184 ) being configured to provide cooling in the subcooled fluid path ( 118 ).
7 . An apparatus as claimed in claim 3 , further comprising:
a sub-cooler ( 122 ); wherein the sub-cooled fluid path ( 118 ) is arranged to pass through the sub-cooler ( 122 ).
8 . An apparatus as claimed in claim 1 , further comprising:
an expander ( 128 ); wherein the expanded fluid path ( 120 ) is arranged to pass though the expander ( 128 ).
9 . An apparatus as claimed in claim 8 , wherein the expander ( 128 ) is arranged to drive a first compressor ( 129 ).
10 . An apparatus as claimed in claim 9 , wherein the fractionating column further comprises:
a nitrogen product fraction tapping point ( 190 ) disposed above the reflux inlet port ( 124 ) and operably coupled to a reflux circuit comprising the first compressor ( 128 ), the reflux circuit returning to the fractionating column ( 116 ) above the nitrogen product fraction tapping point ( 190 ).
11 . An apparatus as claimed in claim 10 , further comprising the sub-cooler ( 122 ) in the reflux circuit.
12 . An apparatus as claimed in claim 4 , further comprising:
a nitrogen return compression and cooling arrangement ( 151 ) disposed in the overhead gas stream path ( 148 ).
13 . An apparatus as claimed in claim 12 , further comprising:
an expander ( 128 ), wherein the expanded fluid path ( 120 ) is arranged to pass through the expander ( 128 ); and wherein the expander ( 128 ) is arranged to drive at least part of the nitrogen return compression and cooling arrangement ( 151 ).
14 . A hydrocarbon capture and recovery system comprising:
the nitrogen recovery apparatus ( 100 ) as claimed in claim 1 ; and a return fluid path fluidly coupling an output port of a nitrogen return compression and cooling arrangement ( 151 ) to a wellbore for returning nitrogen recovered from a natural gas feed and the wellbore under pressure.
15 . A method of recovering nitrogen from natural gas, the method comprising:
separating ( 202 ) a partially liquefied natural gas feed into a vapour fraction and a liquid fraction; splitting ( 206 ) the flow of the vapour fraction to form a first portion and a second portion of vapour fraction; subcooling ( 208 ) the first portion of the vapour fraction using an overhead gas stream ( 148 ) of a fractionating column ( 116 ) to form a reflux stream, the reflux stream being applied to the fractionating column ( 116 ); expanding ( 210 ) the second portion of the vapour fraction to form a middle feed to the fractionating column ( 116 ) below the reflux stream; feeding ( 204 ) the liquid fraction as a bottom feed to the fractionating column ( 116 ); a side-reboiler circuit ( 132 ) feeding the fractionating column ( 116 ) below the bottom feed; and a reboiler circuit ( 140 ) feeding the fractionating column ( 116 ) below the side reboiler circuit.Join the waitlist — get patent alerts
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