Abstract A low temperature method is provided for removing condensable components from an inlet hydrocarbon gas, such as natural gas having a high proportion of methane. The system includes a fractionating column to remove condensed components and a novel reflux step which is arranged to condense additional condensable components from the gas after passing the gas through the fractionating column and to return the additional condensed components back to the fractionating column as reflux. The system utilizes expansion means in the form of a gas turbine which is connected such that the energy generated by the turbine is used to operate a compressor to recompress the gas after removal of certain of the condensable components therefrom.
In a method of removing ethane and heavier components from an inlet hydrocarbon gas comprised principally of methane, the combination of steps comprising: turbine expanding said gas to produce a gas-condensate mixture having a temperature below about -50* F.; fractionally distilling said cooled gas condensate mixture to remove ethane and heavier components therefrom by passing said mixture through a low temperature fractionating column having vertically spaced trays; withdrawing condensed ethane and heavier components from a lower portion of said column; flowing the withdrawn condensed ethane and heavier components to liquid storage; withdrawing fractionally distilled non-condensed gas from a top portion of said column; flowing the fractionally distilled non-condensed gas through a heat exchanger to thereby cool said fractionally distilled gas; flowing additional condensed components from said cooled fractionally distilled gas and flowing said additional condensed components back to said column as reflux; turbine expanding said cooled fractionally distilled non-condensed gas a second time, the turbine expanders of said first and second expanding steps being mechanically connected; flowing twice turbine expanded fractionally distilled non-condensed gas through said heat exchanger as the cooling medium therefor; flowing said twice turbine expanded fractionally distilled non-condensed gas through a second and third heat exchanger as the cooling medium therefor to cool the inlet gas to produce a first gas-condensate mixture and to further cool the non-condensed gas separated from the first gas-condensate mixture to produce a second gas-condensate mixture, the non-condensed gas of which is fed to the first turbine and the separated condensates are fed separately to the column as reflux; and recompressing said twice turbine expanded fractionally distilled non-condensed gas after passage through said heat exchangers.