초록 ▼

The invention is an absorption process for recovering C2+components from a pressurized liquid mixture comprising C1and C2+. The pressurized liquid mixture is at least partially vaporized by heating the liquid mixture in a heat transfer means. The heat transfer means provides refrigeration to an abso

The invention is an absorption process for recovering C2+components from a pressurized liquid mixture comprising C1and C2+. The pressurized liquid mixture is at least partially vaporized by heating the liquid mixture in a heat transfer means. The heat transfer means provides refrigeration to an absorption medium that is used in treating the vaporized mixture in an absorption zone. The vaporized mixture is passed to an absorption zone that produces a first stream enriched in C1and a second stream enriched in C2+components. The pressurized liquid mixture is preferably pressurized liquid natural gas (PLNG) having an initial pressure above about 1,724 kPa (250 psia) and an initial temperature above -112° C. (-170° F.). Before being vaporized, the pressurized liquid mixture is preferably boosted in pressure to approximately the desired operating pressure of the absorption zone.

대표청구항 ▼

1. An absorption method for recovery of C2+components from a pressurized liquid mixture containing C1and C2+,comprising: (a) vaporizing at least part of the pressurized liquid mixture by heating the pressurized liquid mixture in a heat transfer means, said heat transfer means cooling an absorptio

1. An absorption method for recovery of C2+components from a pressurized liquid mixture containing C1and C2+,comprising: (a) vaporizing at least part of the pressurized liquid mixture by heating the pressurized liquid mixture in a heat transfer means, said heat transfer means cooling an absorption medium; and (b) treating the vaporized stream in an absorption zone with the absorption medium to produce a first stream enriched in C1and a second stream enriched in C2+components. 2. The method of claim 1 wherein the pressurized liquid mixture is pressurized liquid natural gas (PLNG). 3. The method of claim 1 wherein the pressurized liquid mixture has an initial pressure above about 1,724 kPa (250 psia) and an initial temperature between about -80° C. (-112° F.) and -112° C. (-170° F.). 4. The method of claim 1 wherein the absorption medium is lean oil. 5. The method of claim 1 wherein the absorption medium is pre-saturated with methane prior to treatment step (b). 6. The method of claim 1 wherein the heat exchange relationship uses a heat-transfer medium being in heat exchange relationship with the liquid mixture in a first heat exchanger and the heat transfer medium being in heat exchange relationship with the absorption stream in a second heat exchanger. 7. The method of claim 1 wherein the heat exchange relationship uses at least one heat exchanger in which the liquid mixture is in indirect contact with the absorption medium. 8. The method of claim 1 further comprises, before passing the pressurized liquid mixture in heat exchange relationship with a heat-transfer stream, heating the liquid mixture by heat exchange relationship with at least one of air, fresh water, and sea water. 9. The method of claim 1 further comprises, after passing the pressurized liquid mixture in heat exchange relationship with a heat-transfer stream, further heating the liquid mixture by heat exchange relationship with at least one of air, fresh water, and sea water. 10. A method for separating C2+components from a pressurized liquid mixture comprising C1and C2+,the method comprising: (a) heating the pressurized liquid mixture to at least partially vaporize the liquid mixture, thereby producing a vapor stream; (b) contacting the vapor stream with an absorbent medium that preferentially absorbs C2+components from the vapor stream; (c) recovering a C1-rich stream substantially depleted of C2+; (d) separating the extracted C2+components from the absorption medium containing the same; (e) cooling at least part of the absorption medium by heat exchange relationship against the pressurized liquid mixture, thereby providing heat for at least partially vaporizing the liquid mixture; and (f) recycling the cooled absorption medium to absorb additional amounts of C2+components.