Abstract An improved process for separating gaseous materials from a mixture containing the same. The process is particularly useful for the separation of high concentrations of nitrogen or similar low boiling materials from hydrocarbon streams such as natural gas and comprises the steps of first liquifying a portion of said gas stream and thereafter separating said stream into a gas phase and a liquid phase in a separation column. The overhead gas stream from the separation column is then passed through one or more turbo-expanders to provide process refrigeration and process energy. In one embodiment, at least a portion of the energy recovered is employed to drive a feed compressor. In a second embodiment, where the feed is at or near the required process pressure, the energy will be available for other purposes. In a third embodiment, where the feed is available at pressures above the required process pressure, the feed may also be passed through one or more suitable turbo-expanders to thereby provide additional process refrigeration as well as additional energy. In all embodiments, the process permits low cost purification. Moreover, depending principally upon feed composition and pressure, surplus energy and refrigeration will be available for other purposes. As will be readily apparent, this constitutes a definite economic credit and thereby permits an even lower cost purification.
A method for separating a non-combustible, nitrogen-rich gaseous feed mixture comprising nitrogen present in the amount of 50 to 80 mole percent and one or more hydrocarbons present in the total amount of 50 to 20 mole percent, into a nitrogen-rich overhead gas product and a combustible hydrocarbon-rich bottom liquid product, said method consisting of the steps of: 1. first cooling said gaseous feed mixture to a temperature below the lowest boiling point of any hydrocarbon present to be separated as a liquid product thereby providing a partially liquefied feed mixture; 2. distilling said partially liquefied feed mixture in a plural stage distillation apparatus so as to form an overhead gas phase and combustible, bottom liquid phase product richer in hydrocarbon then said gaseous feed mixture at a pressure below the critical pressure of both said overhead and bottom products; 3. passing the overhead gas phase directly from the distillation step (2) through turbo-expander means so as to provide an inlet/outlet pressure ratio of between10-1 to 20-1, said ratio being sufficient distillation step (2), in a quantity sufficient to enable recovery of said combustible bottom liquid phase product from said non-combustible feed mixture (4) thereafter using at least a porion of said overhead gas product as a refrigerant to cool the gaseous feed mixture.
Claim 2
Independent Claim
214 words
A method for separating a non-combustible, nitrogen-rich gaseous feed mixture comprising nitrogen present in the amount of 50 to 80 mole percent and one or more hydrocarbons present in the total amount of 50 to 20 mole percent, into a nitrogen-rich overhead gas product and a combustible hydrocarbon-rich bottom liquid product, said method consisting of the steps of: 1. first cooling said gaseous feed mixture to a temperature below the lowest boiling point of any hydrocarbon present to be separated as a liquid product thereby providing a partially liquefied feed mixture; 2. distilling said partially liquefied feed mixture in a plural stage distillation apparatus so as to form an overhead gas phase and combustible, bottom liquid phase product richer in hydrocarbon then said gaseous feed mixture at a pressure below the critical pressure of both said overhead and bottom products; 3. passing the overhead gas phase directly from the distillation step (2) through turbo-expander means so as to provide an inlet/outlet pressure ratio of between10-1 to 20-1, said ratio being sufficient distillation step (2), in a quantity sufficient to enable recovery of said combustible bottom liquid phase product from said non-combustible feed mixture (4) thereafter using at least a porion of said overhead gas product as a refrigerant to cool the gaseous feed mixture.
Claim 3
Dependent Claim
45 words
The method of claim 1 wherein the gaseous feed mixture is a available at a pressure the desired process pressure and the pressure of said feed is increased by passing the same through a compressor driven by the turbo-expander in said overhead gas phase line.