Process and device for the cryogenic separation of a methane-rich stream
In a process for the cryogenic separation of a methane-rich feed stream containing between 3 and 35% of oxygen and also nitrogen, the feed stream is cooled in order to produce a cooled stream, at least one portion of the cooled stream is sent to a distillation column, a bottom stream is withdrawn from the distillation column, the bottom stream being enriched in methane compared to the feed stream, a stream enriched in oxygen compared to the feed stream is withdrawn from the distillation column, and a nitrogen-rich stream is sent to the column.
1. A method for the cryogenic separation of a methane-rich feed stream containing oxygen and nitrogen, the method comprising the steps of:
i) cooling the methane-rich feed stream to produce a cooled stream;
ii) introducing at least a portion of the cooled stream to a distillation column under conditions effective for a distillation of the cooled stream, the distillation column having a distillation section;
iii) withdrawing a bottom stream from the distillation column, the bottom stream being enriched with methane compared with the methane-rich feed stream;
iv) withdrawing an oxygen-enriched stream from the distillation column, the oxygen-enriched stream having a higher percentage of oxygen as compared with the methane-rich feed stream; and
v) introducing a nitrogen-rich gaseous stream coming from an external source to a lower part of the distillation column, such that the nitrogen-rich gaseous stream participates in the distillation of the cooled stream; and
vi) wherein the nitrogen-rich gaseous stream introduced in step v) is in an amount effective to prevent a ternary mixture of methane, oxygen, and nitrogen of having a ternary concentration falling within a flammability zone for the ternary mixture while within the distillation column,
wherein the methane-rich feed stream contains between 3% and 35% oxygen.
2. The method as claimed in claim 1 , wherein the methane-rich feed stream contains between 65% and 97% methane.
3. The method as claimed in claim 1 , wherein the methane-rich feed stream contains between 3% and 35% in total nitrogen and oxygen.
4. The method as claimed in claim 1 , wherein the methane-rich feed stream contains between 3% and 35% nitrogen.
5. The method as claimed in claim 1 , wherein the nitrogen-rich gaseous stream contains at least 90% nitrogen, or even at least 95% nitrogen.
6. The method as claimed in claim 1 , wherein the nitrogen-rich gaseous stream is sent to a bottom of the distillation column, wherein the bottom of the distillation column is a portion of the distillation column that is located below the distillation section.
7. The method as claimed in claim 1 , wherein the methane-rich feed stream is sent to a condenser/reboiler where the methane-rich feed stream is at least partially condensed while partially vaporizing a bottom liquid in order to form a vaporized gas and an at least partially liquefied feed stream, the at least partially liquefied feed stream is sent from the condenser/reboiler to the distillation column and the vaporized gas is mixed with the nitrogen-rich gaseous stream.
8. The method as claimed in claim 1 , wherein a nitrogen-rich liquid stream is vaporized by exchange of heat with the methane-rich feed stream in order to produce the nitrogen-rich gaseous stream.
9. The method as claimed in claim 1 , wherein the methane-rich feed stream contains between 3% and 10% oxygen.
10. A method for the cryogenic separation of a methane-rich feed stream containing oxygen and nitrogen, the method comprising the steps of:
i) cooling the methane-rich feed stream to produce a cooled stream;
ii) introducing at least a portion of the cooled stream to a distillation column under conditions effective for a distillation of the cooled stream to create a bottom stream and a top stream, wherein the bottom stream is enriched with methane compared with the methane-rich feed stream, wherein the top stream is enriched with oxygen as compared with the methane-rich feed stream;
iii) withdrawing the bottom stream from the distillation column;
iv) withdrawing the top stream from the distillation column; and
v) introducing an effective amount of a nitrogen-rich gaseous stream to a lower part of the distillation column, wherein the nitrogen-rich gaseous stream comes from an external source, wherein the effective amount of the nitrogen-rich gaseous stream is based on an amount of nitrogen needed to prevent a ternary mixture of methane, oxygen, and nitrogen of having a ternary concentration falling within a flammability zone for the ternary mixture while within the distillation column,
wherein the methane-rich feed stream contains between 3% and 35% oxygen.