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A process and apparatus for the liquefaction of natural gas including an improved heavy hydrocarbon removal column with overhead condensing and refluxing. Particularly, a methane-rich stream exiting a propane refrigerant cycle is delivered to a heavies removal column, and the heavies depleted vapor

A process and apparatus for the liquefaction of natural gas including an improved heavy hydrocarbon removal column with overhead condensing and refluxing. Particularly, a methane-rich stream exiting a propane refrigerant cycle is delivered to a heavies removal column, and the heavies depleted vapor from the column is at least partially condensed and the liquid portion provided as reflux to the heavies removal column.

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What is claimed is: 1. A method of liquefying natural gas, said method comprising the steps of: (a) cooling the natural gas via indirect heat exchange with a first refrigerant, thereby providing a cooled natural gas stream; (b) using a heavies removal column to separate the cooled natural gas strea

What is claimed is: 1. A method of liquefying natural gas, said method comprising the steps of: (a) cooling the natural gas via indirect heat exchange with a first refrigerant, thereby providing a cooled natural gas stream; (b) using a heavies removal column to separate the cooled natural gas stream into a lights stream and a heavies stream; (c) cooling at least a portion of the lights stream via indirect heat exchange with a second refrigerant of different composition than the first refrigerant, thereby providing a cooled lights stream; (d) separating the cooled lights stream into a predominately liquid phase lights stream and a predominately gas phase lights stream; (e) introducing at least a portion of the predominately liquid phase lights stream into the heavies removal column; and (f) introducing a portion of the natural gas stream into the heavies removal column as a stripping gas, said heavies removal column including a first inlet for receiving the cooled natural gas stream, a second inlet for receiving the predominately liquid phase lights stream, a third inlet for receiving the stripping gas, a first outlet for discharging the lights stream, and a second outlet for discharging the a heavies stream, said first outlet and said second inlet being vertically disposed above the first inlet, said second outlet being vertically disposed below the first inlet, said third inlet being vertically disposed below the first inlet. 2. A method according to claim 1, said first outlet being vertically disposed above the second inlet, said second outlet being vertically disposed below the third inlet. 3. A method according to claim 1, steps (a)-(f) being carried out in a multi-stage cascade-type liquefied natural gas facility using at least three refrigerants, each having a different composition. 4. A method according to claim 1 further comprising the step of vaporizing liquefied natural gas produced via steps (a)-(f). 5. A method according to claim 1, wherein said multi-stage expansion includes flashing the further cooled lights stream to thereby provide a predominately vapor phase and a predominately liquid phase; and using the predominately vapor phase as the predominately methane refrigerant. 6. A method according to claim 1, said first refrigerant comprising predominately propane, propylene, or carbon dioxide. 7. A method according to claim 1, said first refrigerant comprising predominately propane, said second refrigerant comprising predominately ethylene. 8. A method according to claim 1 wherein a cryogenic pump is used to transfer the predominately liquid phase lights stream to the heavies removal column. 9. A method according to claim 1 wherein the at least a portion of the predominately liquid phase lights stream is used as reflux in the heavies removal column. 10. A method according to claim 1; and (g) introducing at least a portion of the predominately liquid phase lights stream into the heavies removal column. 11. A method according to claim 1; and (h) using at least a portion of the predominately liquid phase lights stream as reflux in the heavies removal column. 12. A method according to claim 1; and (i) vaporizing liquefied natural gas produced via steps (a)-(f). 13. An apparatus for liquefying natural gas, said apparatus comprising: a first heat exchanger for cooling the natural gas via indirect heat exchange with a first refrigerant; a heavies removal column positioned downstream of the first heat exchanger and including a first inlet for receiving natural gas, said heavies removal column being operable to separate the natural gas into a lights stream and a heavies stream; a second heat exchanger for cooling the lights stream via indirect heat exchange with a second refrigerant; a separator for separating the cooled stream from the second heat exchanger into a predominately gas phase lights stream and a predominately liquid phase lights stream; an initial heat exchanger positioned upstream of the first heat exchanger and operable to cool the natural gas via indirect heat exchange with the first refrigerant, thereby providing an initially cooled natural gas stream; and a stripping gas heat exchanger for facilitating indirect heat exchange between the initially cooled natural gas stream and the heavies stream, said heavies removal column including a second inlet for receiving the predominately liquid phase lights stream, said heavies removal column including a third inlet for receiving the initially cooled natural gas stream. 14. An apparatus according to claim 13, said first inlet being vertically positioned below the second inlet. 15. An apparatus for liquefying natural gas, said apparatus comprising: a first heat exchanger for cooling the natural gas via indirect heat exchange with a first refrigerant; a heavies removal column positioned downstream of the first heat exchanger and including a first inlet for receiving natural gas, said heavies removal column being operable to separate the natural gas into a lights stream and a heavies stream; a second heat exchanger for cooling the lights stream via indirect heat exchange with a second refrigerant; a separator for separating the cooled stream from the second heat exchanger into a predominately gas phase lights stream and a predominately liquid phase lights stream; and an initial heat exchanger positioned upstream of the first heat exchanger and operable to cool the natural gas via indirect heat exchange with the first refrigerant, thereby providing an initially cooled natural gas stream, said heavies removal column including a second inlet for receiving the predominately liquid phase lights stream, said heavies removal column including a third inlet for receiving the initially cooled natural gas stream, said first inlet being vertically positioned below the second inlet and above the third inlet. 16. An apparatus according to claim 15, said heavies removal column including a first set of internal packing disposed between the first and second inlets, said heavies removal column including a second set of internal packing disposed between the second and third inlets. 17. An apparatus according to claim 15, said heavies removal column including a first outlet for discharging the lights stream and a second outlet for discharging the heavies stream, said first outlet being vertically positioned above the first inlet, said second outlet being vertically position below the third inlet. 18. An apparatus for liquefying natural gas, said apparatus comprising: a first heat exchanger for cooling the natural gas via indirect heat exchange with a first refrigerant; a heavies removal column positioned downstream of the first heat exchanger and including a first inlet for receiving natural gas, said heavies removal column being operable to separate the natural gas into a lights stream and a heavies stream; a second heat exchanger for cooling the lights stream via indirect heat exchange with a second refrigerant; a separator for separating the cooled stream from the second heat exchanger into a predominately gas phase lights stream and a predominately liquid phase lights stream; a third heat exchanger for further cooling at least a portion of the cooled natural gas effluent from the second heat exchanger via indirect heat exchange with the second refrigerant; and a bypass system operable to route at least a portion of the cooled natural gas effluent from the second heat exchanger around the third heat exchanger, said heavies removal column including a second inlet for receiving the predominately liquid phase lights stream. 19. An apparatus according to claim 18, said bypass system including a temperature measuring device and a control valve, said temperature measuring device being operable to generate a temperature signal indicative of the temperature of the cooled natural gas effluent from the third heat exchanger, said control valve being operable to control the amount of natural gas routed around the third heat exchanger based on the temperature signal. 20. An apparatus according to claim 19; and a fourth heat exchanger for cooling at least a portion of the lights stream via indirect heat exchange with the second refrigerant, thereby providing a cooled lights stream. 21. An apparatus according to claim 20; and a fifth heat exchanger for cooling at least a portion of the cooled lights stream via indirect heat exchange with a predominately methane refrigerant, thereby providing a further cooled lights stream. 22. An apparatus according to claim 21, said first refrigerant comprising predominately propane, propylene, or carbon dioxide, said second refrigerant comprising predominately ethane, ethylene, or carbon dioxide. 23. An apparatus according to claim 21, said first refrigerant comprising predominately propane, said second refrigerant comprising predominately ethylene. 24. An apparatus according to claim 21; and a multi-stage expansion cycle operable to cool the further cooled lights stream via sequential pressure reduction. 25. An apparatus according to claim 18; and a cryogenic pump for transferring the predominately liquid phase lights stream from the separator to the second inlet of the heavies removal column. 26. An apparatus according to claim 18, said first and second refrigerants having a different composition. 27. An apparatus according to claim 18, said first refrigerant comprising predominately propane, propylene, or carbon dioxide, said second refrigerant comprising predominately ethane, ethylene, or carbon dioxide. 28. An apparatus according to claim 18, said first refrigerant comprising predominately propane, said second refrigerant comprising predominately ethylene. 29. An apparatus according to claim 18, said apparatus being a cascade-type liquefied natural gas facility having at least three refrigeration cycles, each employing a different refrigerant. 30. An apparatus according to claim 29, said cascade-type liquefied natural gas facility employing an open methane refrigeration cycle. 31. The method according to claim 1, wherein lights stream exiting an upper portion of the heavies removal column and a heavies stream exiting a lower portion of the heavies removal column. 32. The method according to claim 1, wherein cooling at least a portion of the predominately gas phase lights stream in the second refrigeration cycle via indirect heat exchange with the second refrigerant, thereby providing a second cooled natural gas stream. 33. The method according to claim 1, wherein cooling at least a portion of the second cooled natural gas stream in a third refrigeration cycle via indirect heat exchange with a third refrigerant comprising predominately methane. 34. The method according to claim 1, wherein cooling at least a portion of the predominately gas phase lights stream via indirect heat exchange with a predominately methane refrigerant, thereby providing a further cooled lights stream. 35. The method according to claim 1, wherein cooling at least a portion of the further cooled lights stream via multi-stage expansion. 36. The method according to claim 1, wherein said second refrigerant comprises predominately ethane, ethylene, or carbon dioxide.