Liquefaction process for producing subcooled LNG
A variable speed liquid LNG expander (X 1 ) and a variable speed two-phase LNG expander (X 2 ) in line, downstream from X 1 . The rotational speed of both expanders can be controlled and changed independent from each other. The speed of expander X 1 and expander X 2 is determined in such way that the amount of liquid LNG downstream from the PHS compared to the feed gas supply is maximized and the amount of vapor and boil-off downstream of X 2 is minimized.
1. A system for producing optimum sub-cooling of LNG to reduce boil-off losses at a liquefaction plant that produces LNG, the system comprising:
A source of substantially nitrogen-free LNG;
A nitrogen injector for Injecting nitrogen into pressurized natural gas at the liquefaction plant as a first step in sub-cooling the substantially nitrogen-free LNG, thereby producing a nitrogen-rich feed gas supply;
A main heat exchanger for liquefying the nitrogen-rich feed gas supply to form nitrogen-rich, pressurized condensed LNG;
A single-phase liquid expander contained within an initial surrounding vessel under inlet temperature, inlet pressure and inlet mass flow receiving the nitrogen-rich pressurized condensed LNG the single-phase expander having an adjustable rotational speed such that setting a rotational speed of the single-phase expander expands the LNG to outlet pressure, the single-phase expander operable to process the nitrogen-rich pressurized condensed LNG;
A two-phase liquid expander contained within a second surrounding vessel operating in series with the single-phase expander to decrease boil-off gas and optimize a ratio between liquid LNG and vapor LNG, the two-phase expander having an adjustable rotational speed, wherein the two-phase expander is operable to process the nitrogen-rich pressurized condensed LNG received from the single-phase expander and separate the nitrogen from the LNG by evaporation of the nitrogen, the system optimized to produce subcooled liquid LNG to reduce boil-off losses.