Hydrocarbon gas processing

F - Mech Eng,Light,Heat,Weapons – 25 – J

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F25J 3/02 (2006.01) C07C 7/04 (2006.01)

Patent

CA 1309335

ABSTRACT OF THE DISCLOSURE A process for the recovery of ethane and heavier hydrocarbon components from a hydrocarbon gas stream is disclosed. The stream is divided into first and second streams. The first stream is cooled to condense substantially all of it and is thereafter expanded to a pressure below that of the distillation column. After expansion, the cooled first stream is directed in heat exchange relation with a warmer distillation stream rising from fractionation stages of the distillation column. The warmed first stream is then separated to provide a cold vapor and a liquid stream. The liquid is supplied to the column at a first mid-column feed position and the cold vapor is supplied to the column at a second mid-column feed position. The second stream is expanded to the column pressure and is then supplied to the column at a third mid-column feed position. The distillation stream is cooled by the first stream sufficiently to partially condense it. The partially condensed distillation stream is then separated to provide volatile residue gas and a reflux stream feed. The reflux stream feed is supplied to the column at a top column feed position. In instances where the second stream is expanded in a work expansion machine, any condensation formed prior to work expansion is combined either in whole or in part with the first stream prior to cooling and/or expansion, or supplied either in whole or in part to the column as a condensed stream at a fourth mid-column feed position, or some combination thereof. The temperatures of the feeds to the column are effective to maintain the column overhead temperature at a temperature whereby the major portion of the C2+ components is recovered.

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