Liquid natural gas fractionation and regasification plant
View Patent ↗LNG vapor from an LNG storage vessel is absorbed using C 3 and heavier components provided by a fractionator that receives a mixture of LNG vapors and the C 3 and heavier components as fractionator feed. In such configurations, refrigeration content of the LNG liquid from the LNG storage vessel is advantageously used to condense the LNG vapor after separation. Where desired, a portion of the LNG liquid may also be used as fractionator feed to produce LPG as a bottom product.
1. A LNG regasification plant comprising:
a liquefied natural gas storage vessel having a receiving port that is configured to receive liquefied natural gas and further having separate liquid withdrawal and vapor withdrawal ports that are configured to allow separate withdrawal of a liquefied natural gas liquid and a liquefied natural gas vapor from the storage vessel;
a fractionator that is fluidly coupled to the storage vessel and configured to receive a fractionator feed, wherein the fractionator is configured to allow production of (a) an overhead product comprising C 2 and lighter components and (b) a bottom product comprising C 3 and heavier components;
a first conduit configured to combine the bottom product comprising C3 and heavier components with the liquefied natural gas vapor from the storage vessel to thereby form a two-phase mixture;
a heat exchanger configured to condense the two-phase mixture using refrigeration content of the natural gas liquid to thereby form the fractionator feed; and
an overhead condenser coupled to the fractionator and configured to allow refrigeration content of the liquefied natural gas liquid to condense the overhead product comprising C 2 and lighter components; and
a second conduit configured to combine the condensed overhead product comprising C2 and lighter components with the liquefied natural gas liquid to so produce a sendout stream.
2. The plant of claim 1 wherein a portion of the liquefied natural gas vapor from the storage vessel is routed to a second liquefied natural gas storage vessel.
3. The plant of claim 1 further comprising a second heat exchanger configured to heat the fractionator feed using the bottom product comprising C 3 and heavier components from the fractionator as a heat source.
4. The plant of claim 1 wherein the overhead condenser is an internal overhead condenser.
5. The plant of claim 1 further comprising a second liquefied natural gas storage vessel that provides the liquefied natural gas and configured to provide a second liquefied natural gas vapor to the second liquefied natural gas storage vessel.
6. The plant of claim 5 wherein the second liquefied natural gas storage vessel is located on a ship.
7. The plant of claim 1 further comprising a LNG vaporizer that is coupled to the fractionator to receive the sendout stream.
8. The plant of claim 1 wherein the fractionator is further configured to provide a liquefied petroleum gas as a bottom product.
9. The plant of claim 1 wherein the fractionator is configured to receive a portion of the liquefied natural gas liquid as a second fractionator feed after the portion of the liquefied natural gas liquid has provided refrigeration for condensation of the overhead product comprising C 2 and lighter components.
10. A method of handling liquefied natural gas vapor in a LNG regasification plant, comprising:
separately and concurrently withdrawing from a liquefied natural gas storage vessel a liquefied natural gas liquid and a liquefied natural gas vapor;
mixing the liquefied natural gas vapor from the storage vessel with a fractionator bottom product comprising C3 and heavier components to thereby form a two-phase mixture, and condensing the two-phase mixture in a heat exchanger using refrigeration content of the natural gas liquid to so form a fractionator feed;
feeding the fractionator feed into a fractionator to thereby form the fractionator bottom product comprising C3 and heavier components and a stream of C2 and lighter components;
withdrawing the condensed stream of C 2 and lighter components from the fractionator, then
condensing in an overhead condenser the stream of C2 and lighter components using refrigeration content of the liquefied natural gas liquid; and
combining the condensed stream of C2 and lighter components with the liquefied natural gas liquid to so produce a sendout stream.
11. The method of claim 10 further comprising a step of using the fractionator bottom product comprising C 3 and heavier components from the fractionator to heat the fractionator feed before the fractionator feed is fed to the fractionator.
12. The method of claim 10 further comprising a step of providing a second liquefied natural gas storage vessel that provides the liquefied natural gas to the liquefied natural gas storage vessel.
13. The method of claim 12 wherein the second liquefied natural gas storage vessel receives a portion of the liquefied natural gas vapor.
14. The method of claim 12 wherein the second liquefied natural gas storage vessel is configured to form a stream of liquefied natural gas vapor, and wherein the stream of liquefied natural gas vapor is provided back to the second liquefied natural gas storage vessel.
15. The method of claim 12 wherein the second liquefied natural gas storage vessel is located on a ship.
16. The method of claim 10 further comprising a step feeding a portion of the liquefied natural gas liquid to the fractionator after the liquefied natural gas liquid has provided refrigeration for condensation of the C 2 and lighter components.
17. The method of claim 16 wherein the fractionator is configured to provide a liquefied petroleum gas as a bottom product.
18. The method of claim 17 further comprising a step of using a portion of the liquefied natural gas liquid as condensation refrigerant after the liquefied natural gas liquid provided refrigeration for condensation of the C 2 and lighter components.