Method for liquefying methane-rich gas
A method for liquefying methane-rich gas in the form of a feed gas comprising the steps of cooling the gas and partially liquefying the gas by expansion within an expansion device. The pressure of the gas at the inlet of the expansion device is in the range from 40 bar to 100 bar and pressure of the gas at the outlet of the expansion device is in the range from 2 bar to 10 bar.
1. A method for liquefying methane-rich gas in the form of a feed gas comprising the steps of cooling the gas and partially liquefying the gas by expansion within an expansion device, wherein the pressure of the gas at the inlet of the expansion device is in the range from 40 bar to 100 bar and the pressure of the gas at the outlet of the expansion device is in the range from 4 bar to 10 bar.
2. A method according to claim 1 , wherein the pressure of the gas at the outlet of the expansion device is in the range from 4 bar to 6 bar.
3. A method according to claim 2 , wherein the pressure of the gas at the outlet of the expansion device is substantially 5 bar.
4. A method according to claim 1 , wherein the pressure of the gas at the inlet of the expansion device is in the range from 40 bar up to a pressure below the critical pressure of the gas.
5. A method according to claim 4 , wherein the pressure of the gas at the inlet of the expansion device is in the range from 45 bar up to a pressure below the critical pressure of the gas.
6. A method according to claim 1 , comprising cooling the methane-rich gas in at least one heat exchange device.
7. A method according to claim 6 , wherein the at least one heat exchange device utilizes additional refrigeration means.
8. A method according to claim 7 , wherein the additional refrigeration means comprises a substantially closed circuit refrigeration system of cycling refrigerant material.
9. A method according to claim 8 , comprising the additional steps of removing a by-product material and processing the by-product material to produce refrigerant material to fill and/or compensate for losses of material from the substantially closed circuit refrigeration system.
10. A method according to claim 9 , comprising obtaining the by-product material by separating material from a flash gas.
11. A method according to claim 9 , comprising obtaining the by-product material by processing the feed gas.
12. A method according to claim 9 , wherein the by-product material comprises compounds selected from the group consisting of propane, butane, and heavier hydrocarbon compounds.
13. A method according to claim 9 , comprising flashing the by-product material within a flash vessel to produce a refrigerant vapor.
14. A method according to claim 13 , wherein the by-product material entering the flash vessel has a pressure in a range from 20 bar to 1 bar.
15. A method according to claim 14 , wherein the by-product material entering the flash vessel has a pressure in a range from 10 bar to 5 bar.
16. A method according to claim 13 , wherein the by-product material entering the flash vessel is at a temperature in a range from −20 degrees Celsius to 60 degrees Celsius.
17. A method according to claim 16 , wherein the by-product material entering the flash vessel is at a-temperature in a range from 20 degrees Celsius to 40 degrees Celsius.
18. A method according to claim 13 , comprising incorporating the vapor into the refrigerant material of the substantially closed circuit refrigeration system.
19. A method according to claim 1 , comprising cooling the methane-rich gas to a temperature in a range from −50 degrees Celsius to 5 degrees Celsius below its dew point, prior to entry the expansion device.
20. A method according to claim 19 , comprising cooling the methane-rich gas to a temperature substantially equivalent to its dew point, prior to entry into the expansion device.
21. A method according to claim 1 , wherein the methane-rich gas is outside a phase equivalent to its dense phase prior to entry into the expansion device.