초록 ▼

This invention is a method and apparatus for production of pressurized liquefied gas. First, a gas stream is cooled and expanded to liquefy the gas stream. The liquefied gas stream is then withdrawn as pressurized gas product and a portion is recycled through the heat exchanger to provide at least p

This invention is a method and apparatus for production of pressurized liquefied gas. First, a gas stream is cooled and expanded to liquefy the gas stream. The liquefied gas stream is then withdrawn as pressurized gas product and a portion is recycled through the heat exchanger to provide at least part of the cooling and is returned to the stream. Recycling the pressurized liquefied gas product helps keep the cooling and compression of the gas stream in the supercritcal region of the phase diagram. J-T valves in parallel with the expander permits running the system until the stream is in the supercritical region of its phase diagram and the hydraulic expander can operate. This process is suitable for natural gas streams containing methane to form a pressurized liquefied natural gas (PLNG) product.

대표청구항 ▼

1. A process for liquefying a gas stream by compressing, cooling and expansion of the gas stream in the supercritical region of the phase diagram, comprising:(a) compressing the gas stream into the supercritical region of its phase diagram;(b) cooling the supercritical gas stream to a temperature le

1. A process for liquefying a gas stream by compressing, cooling and expansion of the gas stream in the supercritical region of the phase diagram, comprising:(a) compressing the gas stream into the supercritical region of its phase diagram;(b) cooling the supercritical gas stream to a temperature less than the gas stream's critical temperature to form a supercritical dense phase fluid;(c) expanding the supercritical dense phase fluid stream without traversing the gas stream's critical point during expansion;(d) removing the expanded gas stream from the process as a liquid product; and(e) recycling a portion of the liquefied product to provide a portion of the cooling of step (b). 2. The process of claim 1 wherein the gas stream contains methane. 3. The process of claim 1 wherein the gas stream is cooled in at least one heat exchanger. 4. The process of claim 1 wherein the gas stream is expanded in step (c) in at least one hydraulic expander. 5. The process of claim 1 wherein the gas stream is expanded in step (c) with at least one J-T valve. 6. The process of claim 1 wherein the gas is expanded in step (c) with a combination of at least one hydraulic expander and at least one J-T valve. 7. The process of claim 1 wherein the fluid stream is expanded in step (c) in at least one J-T valve until the stream becomes a dense fluid and then the stream is expanded in at least one hydraulic expander. 8. The process of claim 1 wherein the liquefied product is pressurized liquefied natural gas. 9. Pressurized liquefied gas produced according to the process of claim 1. 10. A process for producing a liquid gas product comprising:(a) providing a gas stream having a pressure of at least 9,315 kPa (1350 psia);(b) cooling the gas stream to create a supercritical dense phase fluid stream;(c) withdrawing a portion of the supercritical dense phase fluid stream and expanding the withdrawn supercritical dense phase fluid stream and using the expanded stream to provide a portion of the cooling for step b;(d) expanding the remaining portion of the cooled supercritical dense phase fluid stream to a lower pressure and a temperature below the critical temperature of the gas stream to produce a liquefied product; and(e) recycling a portion of the liquefied product to provide a portion of the cooling for step b. 11. The process of claim 10 wherein the gas stream contains methane. 12. The process of claim 10 wherein the gas stream is cooled in at least one heat exchanger. 13. The process of claim 10 wherein the gas stream is expanded in steps (c) and (d) in at least one hydraulic expander. 14. The process of claim 10 wherein the gas stream is expanded in steps (c) and (d) with at least one J-T valve. 15. The process of claim 10 wherein the gas is expanded in steps (c) and (d) with a combination of at least one hydraulic expander and at least one J-T valve. 16. The process of claim 10 wherein the gas stream is expanded in steps (c) and (d) in at least one J-T valve until the stream becomes a dense fluid and then the stream is expanded in at least one hydraulic expander. 17. The process of claim 10 wherein the liquefied product is pressurized liquefied natural gas. 18. The process of claim 10 wherein said gas stream in the supercritical region is at a lower temperature than the critical temperature of the gas stream. 19. A process for liquefying a pressurized gas stream, which comprises:(a) withdrawing a first fraction of the pressurized gas stream thereby leaving a second fraction and expanding the withdrawn first fraction to a lower pressure to cool and at least partially liquefy the withdrawn first fraction;(b) cooling the second fraction of the pressurized gas stream by indirect heat exchange with the expanded first fraction;(c) expanding the second fraction of the pressurized gas stream to a lower pressure, thereby at least partially liquefying the second fraction of the pressurized gas stream;(d) removing a portion of the liquefied second fraction from the process as a pressurized product stream having a pressure at or above its bubble point pressure; and(e) recycling a portion of the liquefied second fraction from the pressurized product stream to provide a portion of the cooling in step (b). 20. The process of claim 19 wherein the gas stream contains methane. 21. The process of claim 19 wherein the gas stream is cooled in at least one heat exchanger. 22. The process of claim 19 wherein the gas stream is expanded in steps (a) and (c) in at least one hydraulic expander. 23. The process of claim 19 wherein the gas stream is expanded in steps (a) and (c) with at least one J-T valve. 24. The process of claim 19 wherein the gas is expanded in steps (a) and (c) with a combination of at least one hydraulic expander and at least one J-T valve. 25. The process of claim 19 wherein the gas stream is expanded in steps (a) and (c) in at least one J-T valve until the stream becomes a dense fluid stage and then the stream is expanded in at least one hydraulic expander. 26. The process of claim 19 wherein the liquefied product is pressurized liquefied natural gas. 27. A process for liquefying a pressurized gas stream to create a pressurized liquefied gas product by compressing, cooling and expansion of the gas stream in the supercritical region of the phase diagram at temperatures lower than the critical temperature of the stream, comprising:(a) compressing a gas stream to a pressure of at least 9,315 kPa (1,350 psia) and cooling the gas stream to a temperature of at least 41° C. (105° F.);(b) cooling the pressurized gas stream in a first heat exchanger by indirect heat exchange with the expanded first fraction from step (c) and the vapor and pressurized liquefied gas product from step (h);(c) withdrawing a first fraction from the cooled gas stream of step (b), thereby leaving a second fraction of the pressurized gas stream, and expanding the withdrawn first fraction to a lower pressure to cool and at least partially liquefy the first fraction;(d) cooling the second fraction of the pressurized gas stream in a second heat exchanger by indirect heat exchange with the vapor and pressurized liquefied gas product from step (h);(f) pressure expanding the second fraction to a lower pressure, thereby at least partially liquefying the second fraction of the pressurized gas stream;(g) passing the expanded second fraction of step (f) to a phase separator which separates vapor produced by the expansion of step (f) from liquid produced by such expansion;(h) removing vapor and a portion of the liquefied gas product from the phase separator and passing the vapor and the pressurized liquefied gas product in succession through the second heat exchanger and then the first heat exchanger;(i) compressing and cooling the vapor and pressurized liquefied gas exiting the first heat exchanger and returning the compressed, cooled vapor and pressurized liquefied gas to the pressurized stream for recycling; and(j) removing from the phase separator a pressurized liquefied product. 28. The process of claim 27 wherein the gas stream contains methane. 29. The process of claim 27 wherein the gas stream is expanded in steps (c) and (f) in at least one hydraulic expander. 30. The process of claim 27 wherein the gas stream is expanded in steps (c) and (f) with at least one J-T valve. 31. The process of claim 27 wherein the gas is expanded in steps (c) and (f) with a combination of at least one gas expander and at least one J-T valve. 32. The process of claim 27 wherein the gas stream is expanded in steps (c) and (f) in at least one J-T valve until the stream becomes a dense fluid stage and then the stream is expanded in at least one hydraulic expander. 33. The process of claim 27 wherein the liquefied product is pressurized liquefied natural gas. 34. A process for liquefying a pressurized gas stream to create a pressurized liquefied gas product by compressing, cooling and expansion of the gas stream in the supercr itical region of the phase diagram at temperatures lower than the critical temperature of the stream, comprising:(a) compressing a gas stream to a pressure of at least 9,315 kPa (1,350 psia) and cooling the gas stream to a temperature of at least 41° C. (105° F.);(b) cooling the pressurized gas stream in a first heat exchanger by indirect heat exchange;(c) withdrawing a first fraction from the cooled gas stream of step (b), thereby leaving a second fraction of the pressurized gas stream, and expanding the withdrawn first fraction to a lower pressure to cool and at least partially liquefy the first fraction in step (b);(d) cooling the second fraction of the pressurized gas stream in a second heat exchanger by indirect heat exchange;(e) pressure expanding the second fraction to a lower pressure, thereby at least partially liquefying the second fraction of the pressurized gas stream;(f) passing the expanded second fraction of step (f) to a phase separator which separates vapor produced by the expansion of step (f) from liquid produced by such expansion;(g) removing vapor and a portion of the liquefied gas product from the phase separator and passing the vapor and the pressurized liquefied gas product in succession through the second heat exchanger in step (d) and then the first heat exchanger in step (b);(h) compressing and cooling the vapor and pressurized liquefied gas exiting the first heat exchanger and returning the compressed, cooled vapor and pressurized liquefied gas to the pressurized stream for recycling; and(i) removing from the phase separator a pressurized liquefied product. 35. An apparatus for liquefying a gas stream, comprising:(a) means for compressing the gas stream to the supercritical dense phase region of its phase diagram;(b) means for cooling the fluid without traversing the gas stream's critical point during cooling;(c) means for expanding the fluid without traversing the gas stream's critical point during expansion;(d) means for removing the expanded gas stream as a liquid product; and(e) means for recycling a portion of the liquefied product to provide a portion of the cooling for step (b). 36. The apparatus of claim 35 wherein the means for cooling is at least one heat expander. 37. The apparatus of claim 35 wherein the means for expanding is at least one gas expander. 38. The apparatus of claim 35 wherein the means for expanding is at least one J-T valve. 39. The apparatus of claim 35 wherein the means for expanding is a combination of at least one gas expander and at least one J-T valve. 40. The apparatus of claim 35 wherein the apparatus further comprises means for withdrawing a fraction of the gas stream, means for expanding the withdrawn gas stream to cool the withdrawn gas stream and means for using the withdrawn and expanded gas stream to provide a portion of the cooling in step (b).