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A method of liquefying a hydrocarbon stream such as natural gas from a feed stream, the method at least comprising the steps of: (a) providing a feed stream (10); (b) dividing the feed stream (10) of step (a) to provide at least a first feed stream (20) comprising at least 90 mass % of the initial f

A method of liquefying a hydrocarbon stream such as natural gas from a feed stream, the method at least comprising the steps of: (a) providing a feed stream (10); (b) dividing the feed stream (10) of step (a) to provide at least a first feed stream (20) comprising at least 90 mass % of the initial feed stream (10), and a second feed stream (30); (c) liquefying the first feed stream (20) of step (b) at a pressure between 20-100 bar to provide a first liquefied natural gas (LNG) stream (40); (d) cooling the second feed stream (30) of step (b) to provide a cooled feed stream (50); (e) combining the first LNG stream (40) of step (c) with the cooled feed stream (50) of step (d) to provide a combined LNG stream (60); (f) reducing the pressure of the combined LNG stream (60) of step (e); and (g) passing the combined LNG stream (60) of step (f) through a flash vessel (12) to provide a product LNG stream (70) and a gaseous stream (80).

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1. A method of liquefying a hydrocarbon stream from a feed stream, the method at least comprising the steps of: (a) providing a feed stream;(b) dividing the feed stream of step (a) to provide at least a first feed stream comprising at least 90% of the mass of the initial feed stream, and a second fe

1. A method of liquefying a hydrocarbon stream from a feed stream, the method at least comprising the steps of: (a) providing a feed stream;(b) dividing the feed stream of step (a) to provide at least a first feed stream comprising at least 90% of the mass of the initial feed stream, and a second feed stream;(c) liquefying the first feed stream of step b) in a first heat exchanger at a pressure between 20 bar and 100 bar to provide a first liquefied natural gas (LNG) stream;(d) cooling the second feed stream of step b) in a second heat exchanger to provide a cooled feed stream;(e) combining the first LNG stream of step (c) with the cooled feed stream of step (d) to provide a combined LNG stream consisting essentially of liquid;(f) reducing the pressure of the combined LNG stream of step (e) by passing the combined LNG stream consisting essentially of liquid through an expander that creates work energy for use elsewhere in the method; and(g) passing the combined LNG stream of step (f) through a flash vessel to provide a product LNG stream and a gaseous stream that is used in the method without recycling to the feed stream. 2. The method as claimed in claim 1 wherein the first feed stream comprises at least 95% of the mass of the initial feed stream. 3. The method as claimed in claim 1 wherein the second feed stream is cooled in step (d) to a temperature of at least −100° C. 4. The method as claimed in claim 1 wherein the second feed stream is between 1% by mass and 5% by mass of the feed stream containing natural gas. 5. The method as claimed in claim 1 wherein the pressure of the product LNG stream is between 1 bar and 10 bar. 6. The method as claimed claim 1 wherein there is no significant pressure change other than any de minimis change of 10 bar or less of the first feed stream between said dividing in step (b) and said combining in step (e). 7. A method as claimed in claim 1 wherein the first feed stream comprises at least 97% of the mass of the initial feed stream. 8. The method as claimed in claim 1, wherein step g) further comprises passing the combined LNG stream of step f) through a flash valve, prior to passing it through the flash vessel. 9. The method as claimed in claim 1 further comprising the step of: (h) passing the second feed stream and the gaseous stream through the second heat exchanger to at least partly provide the cooling of the second feed stream in step (d). 10. The method as claimed in claim 9 wherein the temperature of the gaseous stream after passing through the second heat exchanger for step (d) is between 30° C. and 50° C. 11. The method as claimed in claim 9 further comprising the step of: (i) using the gaseous stream outputted from the second heat exchanger as a fuel gas stream. 12. A method as claimed in claim 9 wherein the first feed stream comprises at least 95% of the mass of the initial feed stream. 13. The method as claimed in claim 9 wherein the second feed stream is cooled in step (d) to a temperature of −100° C. or below. 14. The method as claimed in claim 9 further comprising the step of: (i) using the gaseous stream outputted from the second heat exchanger as a fuel gas stream. 15. A method as claimed in claim 14 wherein the first feed stream comprises at least 95% of the mass of the initial feed stream. 16. The method as claimed in claim 9 further comprising the step of passing the gaseous stream through one or more additional heat exchangers. 17. The method as claimed in claim 16 wherein the temperature of the gaseous stream after passing through the first heat exchanger is above 0° C. 18. The method as claimed in claim 16 wherein the first feed stream comprises at least 95% of the mass of the initial feed stream. 19. The method as claimed in claim 16 wherein the second feed stream is cooled in step (d) to a temperature of −100° C. or below. 20. An apparatus for producing a liquefied hydrocarbon gas from a feed stream, the apparatus at least comprising: a stream splitter configured to divide the feed stream into at least a first feed stream comprising at least 90% of the mass of the initial feed stream, and a second feed stream;a liquefying system including at least a first heat exchanger configured to liquefy the first feed stream at a pressure between 20 bar and 100 bar to provide a first liquefied natural gas (LNG) stream;a second heat exchanger configured to at least partly cool the second feed stream to provide a cooled feed stream;a combiner configured to combine the first LNG stream and the cooled feed stream so as to provide a combined LNG stream consisting essentially of liquid;an expander configured to reduce the pressure of the combined LNG stream thereby creating work energy for use elsewhere in the apparatus; anda flash vessel configured to provide a product LNG stream and a gaseous stream for use in the apparatus without recycling to the feed stream. 21. The apparatus as claimed in claim 20 wherein the apparatus further comprises a conduit to pass the gaseous stream through the second heat exchanger.