초록 ▼

A cryogenic separation process for rejecting carbon dioxide from a carbon-dioxide-containing natural gas mixture. The invention is specifically designed for treating a natural gas mixture recovered from a petroleum well employing the enhanced recovery technique of carbon dioxide flooding. The carbon

A cryogenic separation process for rejecting carbon dioxide from a carbon-dioxide-containing natural gas mixture. The invention is specifically designed for treating a natural gas mixture recovered from a petroleum well employing the enhanced recovery technique of carbon dioxide flooding. The carbon-dioxide-containing natural gas mixture is treated using a particular arrangement of fractional condensation, partial vaporization and rectification unit operations to produce an enriched-methane gas stream and carbon dioxide product streams at various pressures. The invention is well suited for the bulk separation of large quantities of carbon dioxide from carbon-dioxide-containing natural gas mixtures, as a preparatory step for the subsequent purification of the enriched-methane product by conventional absorption techniques.

대표청구항 ▼

A method for separating carbon dioxide from a carbon-dioxide-containing natural gas mixture having a high carbon dioxide content comprising: (1) providing a natural gas mixture containing about 10 to 70% methane and having a carbon dioxide content of 30 to 90 mol percent and liquefying a major porti

A method for separating carbon dioxide from a carbon-dioxide-containing natural gas mixture having a high carbon dioxide content comprising: (1) providing a natural gas mixture containing about 10 to 70% methane and having a carbon dioxide content of 30 to 90 mol percent and liquefying a major portion of the carbon dioxide in the natural dioxide in the natural gas mixture by cooling the gas mixture, at an elevated pressure above about 700 psig, (2) thereafter separating the cooled natural gas mixture of step (1) into a condensed liquid carbon-dioxide-containing stream and non-condensed vapor, (3) subcooling the liquid carbon-dioxide-containing stream, (4) rectifying the subcooled liquid carbon-dioxide-containing stream to provide methane-containing overhead vapor and a kettle liquid having an increased carbon dioxide content, (5) vaporizing a minor portion of the carbon-dioxide-containing kettle liquid of step (4) by heating so as to provide reflux vapor for rectifying the subcooled liquid carbon-dioxide-containing stream of step (4), (6) separating a carbon-dioxide-enriched liquid from the vapor of step (5), (7) combining the methane-containing overhead vapor separation of step (4) with the non-condensed vapor separated in step (2) to provide a methane-containing gas mixture, (8) cooling the methane-containing gas mixture of step (7) and rectifying the cooled mixture to provide a methane-enriched overhead vapor and a kettle liquid containing carbon dioxide, the steps (1) through (8) being conducted at a pressure below the critical pressure and at a temperature above the triple point temperature for each composition involved.