Selective removal of nitrogen from natural gas by pressure swing adsorption
First Claim
1. A pressure swing absorption (PSA) process for the separation of nitrogen from a mixture of the same with methane which comprises:
- (a) passing a feed stream comprising said mixture in contact with a nitrogen-selective sorbent in a PSA unit so as to preferentially adsorb nitrogen and produce a methane-rich product stream containing at least 70 mol. % methane and a low pressure purge stream having a higher molar concentration of nitrogen than said mixture; and
(b) subsequent to step (a), periodically heating said nitrogen-selective sorbent with the methane-rich product stream to drive off accumulated methane from such sorbent.
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Abstract
A pressure swing adsorption process for the separation of nitrogen from natural gas utilizes two separate pressure swing adsorption stages, the first containing a hydrocarbon-selective adsorbent and the second containing a nitrogen-selective adsorbent. In the process, the product stream from the first pressure swing adsorption unit contains a natural gas stream having a reduced hydrocarbon content and the product stream from the second pressure swing adsorption unit is a natural gas stream having a reduced nitrogen concentration. The product from the second pressure swing adsorption unit is used to desorb the hydrocarbons from the first pressure swing adsorption unit so as to add the hydrocarbons, which have heat value to the product natural gas stream. Periodically, heating the nitrogen-selective adsorbent with heated product stream from the second pressure swing adsorption unit has been found to improve the capacity of the nitrogen-selective adsorbent to adsorb nitrogen.
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Citations
38 Claims
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1. A pressure swing absorption (PSA) process for the separation of nitrogen from a mixture of the same with methane which comprises:
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(a) passing a feed stream comprising said mixture in contact with a nitrogen-selective sorbent in a PSA unit so as to preferentially adsorb nitrogen and produce a methane-rich product stream containing at least 70 mol. % methane and a low pressure purge stream having a higher molar concentration of nitrogen than said mixture; and
(b) subsequent to step (a), periodically heating said nitrogen-selective sorbent with the methane-rich product stream to drive off accumulated methane from such sorbent. - View Dependent Claims (2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13)
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14. A process for the separation of nitrogen and hydrocarbons from a natural gas stream, which comprises:
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passing said natural gas stream to a first pressure swing adsorption unit containing a hydrocarbon-selective sorbent so as to preferentially adsorb at least C4+ hydrocarbons to produce a first product stream comprising methane, nitrogen and a reduced level of said hydrocarbons relative to said natural gas stream; and
passing said first product stream to a second pressure swing absorption unit containing a nitrogen-selective sorbent so as to preferentially adsorb nitrogen and produce a second product stream enriched with methane and a low pressure purge stream having a higher molar concentration of nitrogen than said first product stream. - View Dependent Claims (15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, 29, 30, 31, 32, 33, 34)
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35. A pressure swing absorption (PSA) process for the separation of nitrogen from a mixture of the same with methane which comprises:
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(a) passing a feed stream comprising said mixture in contact with a nitrogen-selective sorbent in a PSA unit so as to preferentially adsorb nitrogen and produce a methane-rich product stream containing at least 70 mol. % methane and a low pressure purge stream having a higher molar concentration of nitrogen than said mixture; and
(b) co-currently depressurizing said PSA unit to form a recycle stream rich in methane, said recycle stream having a pressure less than said methane-rich product stream, but greater than said purge stream, recycling said recycle stream to said feed stream. - View Dependent Claims (36, 37, 38)
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Specification