NOVELTY - Production of liquefied natural gas (LNG) and gas to liquid (GTL) products involves processing cooled natural gas stream in at least two expansion/separation cycles, and converting a portion of the cycle natural gas vapor components into a GTL product. Each cycle comprises isentropically or isenthalpically expanding a portion of the cooled natural gas stream, and producing and separating a natural gas vapor component and a LNG component.    USE - The process is used for producing liquefied natural gas (LNG) (claimed) and gas to liquid (GTL) products.    ADVANTAGE - Directing an expanded natural gas vapor for GTL conversion, available at more favorable conditions of pressure and temperature, from higher pressure expansion and separation steps, provides energy and capital savings compared to processes which require separate facilities for compressing and heating a natural gas vapor present at near atmospheric pressure and colder temperatures. Performing at least two expansion and separation cycles subsequent to removal of NGLs from a cooled natural gas stream permits the plant operator to customize and improve the quality of the LNG product produced compared to LNG product produced from a single expansion and separation cycle constrained to a final atmospheric LNG separation step.    DETAILED DESCRIPTION - Production of liquefied natural gas and gas to liquid products involves cooling natural gas (1) in at least one cooling step (2) to provide a cooled natural gas stream (8), processing the cooled natural gas stream in at least two expansion/separation cycles, and converting at least a portion of at least one of the expansion/separation cycle natural gas vapor components (13A) into a GTL product. Each expansion/separation cycle comprises isentropically or isenthalpically expanding at least a portion of the cooled natural gas stream and producing a natural gas vapor component and a LNG component (19), separating at least a portion of the natural gas vapor component from the LNG component, and repeating these steps. At least a portion of the LNG component from the previous expansion/separation cycle is directed to each successive isentropic or isenthalpic expansion (9) step. The final LNG product is the LNG component after the final separating step and is liquid at atmospheric pressure.    DESCRIPTION OF DRAWING(S) - The figure shows an integrated process for producing LNG and GTL products.    Natural gas (1)    Cooling step (2)    Cooled natural gas stream (8)    Isentropic or isenthalpic expansion (9)    Natural gas vapor components (13A)    LNG component (19)