Method and system for optimized LNG production
A method and system for producing liquefied and sub-cooled natural gas by means of a refrigeration assembly using a single phase gaseous refrigerant comprising: at least two expanders ( 1 - 3 ); a compressor assembly ( 5 - 7 ); a heat exchanger assembly ( 8 ) for heat absorption from natural gas; and a heat rejection assembly ( 10 - 12 ). The novel features according to the present invention are arranging the expanders ( 1 - 3 ) in expander loops; using only one and the same refrigerant in all loops; passing an expanded refrigerant flow from the respective expander into the heat exchanger assembly ( 8 ), each being at a mass flow and temperature level adapted to de-superheating, condensation or cooling of dense phase and/or sub-cooling of natural gas; and serving the refrigerant to the respective expander in a compressed flow by means of the compressor assembly having compressors or compressor stages enabling adapted inlet and outlet pressures for the respective expander.
1. A method for producing liquefied and sub-cooled natural gas using a refrigeration assembly comprising a single phase gaseous refrigerant and comprising at least two refrigeration cycles each comprising an expander arranged in an expander loop, wherein a single-component refrigerant is used as the refrigerant in all expander loops, a compressor assembly, a heat exchanger structure for heat absorption from natural gas, a heat rejection assembly and an inventory vessel, the method comprising:
passing an expanded refrigerant flow from each respective expander into the heat exchanger structure, each expander being at a mass flow and temperature level adapted to perform de-superheating, condensation or cooling of dense phase and/or sub-cooling of natural gas; and
serving the refrigerant to each respective expander in a compressed flow using the compressor assembly having compressors or compressor stages enabling adapted inlet and outlet pressures for each respective expander,
wherein each of the refrigeration cycles is connected to the inventory vessel, and
refrigeration capacities of the refrigeration cycles are controlled independently from each other by varying refrigerant inventories of the refrigeration cycles using the inventory vessel and valves.
2. The method of claim 1 , wherein the refrigerant comprises nitrogen.
3. The method of claim 1 , wherein the expanders are connected to the compressor assembly as to fluidly form an integrated refrigeration assembly with separate expander loops.
4. The method of claim 1 , wherein each expander is connected to the compressor assembly as to fluidly form separate refrigeration cycles.
5. The method of claim 1 , wherein refrigeration capacities are independently varied in each of at least two cycles by separate inventory control.
6. The method of claim 5 , wherein the refrigeration capacities are controlled by compressor speed control.
7. The method of claim 1 , wherein two or more expanders are connected in series with intermediate cooling between expander stages.
8. A system for producing liquefied and sub-cooled natural gas comprising a refrigeration assembly using a single phase gaseous refrigerant, the refrigeration assembly comprising:
at least two refrigeration cycles each comprising an expander;
a compressor assembly;
a heat exchanger structure for heat absorption from natural gas;
a heat rejection assembly; and
an inventory vessel, wherein
the expanders are arranged in expander loops, a single-component refrigerant is used as the refrigerant in all loops, an expanded refrigerant flow from each respective expander is passed into the heat exchanger structure, each respective expander being at a mass flow and temperature level adapted to perform de-superheating, condensation or cooling of dense phase and/or sub-cooling of natural gas;
the refrigerant to each respective expander is served in a compressed flow using the compressor assembly having compressors or compressor stages enabling adapted inlet and outlet pressures for each respective expander;
each of the refrigeration cycles is connected to the inventory vessel, and
refrigeration capacities of the refrigeration cycles are controlled independently from each other by varying refrigerant inventories of the refrigeration cycles using the inventory vessel and valves.
9. The system according to claim 8 , wherein the refrigerant comprises nitrogen.
10. The system of claim 8 , wherein the expanders are connected to the compressor assembly as to fluidly form an integrated refrigeration assembly with separate expander loops.
11. The system of claim 8 , wherein each expander is connected to the compressor assembly as to fluidly form separate refrigeration cycles.
12. The system of claim 8 , wherein refrigeration capacities are independently varied in each cycle by separate inventory control.
13. The system of claim 12 , wherein the refrigeration capacities are controlled by compressor speed control.
14. The system of claim 8 , comprising two or more expanders connected in series with intermediate cooling between expander stages.