Method for purifying natural gas using an economizer
A process for purifying a gaseous feed stream of natural gas including methane, CO 2 and heavy hydrocarbons including step a): cooling the gaseous feed stream in a heat exchanger; step b): introducing the cooled stream into a phase-separating chamber to produce a liquid stream depleted in methane and enriched in heavy hydrocarbons and a gaseous stream; step c): separating the gaseous stream obtained from step b) in a first membrane producing at least one CO 2 -enriched permeate stream and a residual stream enriched in methane; step d): introducing the residual stream obtained from step c) into a phase-separator to produce a liquid stream and a gaseous stream; step e): heating the gaseous stream obtained from step d) by introducing it into the heat exchanger used in step a) counter-currentwise with the feed stream thereby producing a gaseous stream depleted in CO 2 and enriched in methane.
1. A process for purifying a gaseous feed stream of natural gas comprising methane, CO 2 and hydrocarbons containing at least two carbon atoms, comprising the following steps:
Step a): cooling the gaseous feed stream in a heat exchanger;
Step b): introducing stream obtained from step a) into a phase-separating chamber to produce a liquid stream depleted in methane and enriched in hydrocarbons containing more than three carbon atoms and a gaseous stream;
Step c): separating the gaseous stream obtained from step b) in a first membrane permeation unit including at least one main membrane separation stage from which emerges at least one CO 2 -enriched gaseous first permeate stream and a partially condensed first residual stream depleted in CO 2 and enriched in methane;
Step d): introducing the first residual stream obtained from step c) into a phase-separating chamber to produce at least two phases, a liquid stream including at least 0.5 mol % of hydrocarbons containing at least three carbon atoms initially contained in the feed stream, and a gaseous stream;
Step e): heating the gaseous stream obtained from step d) by introducing it into the heat exchanger used in step a) counter-currentwise relative to the feed stream so as to produce a gaseous stream depleted in CO 2 and enriched in methane relative to the feed stream; and
Step f): introducing the gaseous stream obtained from step e) into a second membrane separation unit, from which emerges at least one gaseous second permeate stream enriched in CO 2 and a gaseous second residual stream depleted in CO 2 and enriched in methane.
2. The process as claimed in in claim 1 , wherein the second residual stream contains less than 8 mol % of CO 2 and more than 80 mol % of methane.
3. The process as claimed in claim 1 , wherein the gaseous stream obtained from step d) undergoes Joule-Thomson expansion prior to step e).
4. The process as claimed in claim 1 , wherein the feed stream to be purified comprises at least 15 mol % of CO 2 .
5. The process as claimed in claim 1 , wherein the gaseous stream obtained from step e) is heated by introducing it into a heating means so as to produce a gaseous stream prior to step f).
6. The process as claimed in claim 1 , wherein the liquid stream obtained from step b) is introduced into the heat exchanger used in step a) counter-currentwise relative to the feed stream.
7. The process as claimed in claim 1 , wherein the liquid stream obtained from step d) is mixed with the liquid stream obtained from step b) before being introduced into the heat exchanger used in step a) counter-currentwise relative to the feed stream.