Method for gas separation

Patent metadata

Field	Value
Publication number	US-10279305-B2
Application number	US-201615566434-A
Country	US
Kind code	B2
Filing date	Apr 15, 2016
Priority date	Apr 15, 2015
Publication date	May 7, 2019
Grant date	May 7, 2019

Abstract

A method for controlling gas separation of a gas mixture comprising a first component and a second component, the method comprising contacting a feed containing the gas mixture with an adsorbent in a bed in a column in a dual reflux swing adsorption process such that a first component of a gas mixture attains or exceeds a desired purity and a second component of the gas mixture attains or exceeds a desired purity, wherein the mathematical product of the cycle feed time and the sum of the molar feed flow rate and the molar reflux flow rate directed to the column does not exceed the maximum number of moles that can be treated per bed per cycle and wherein the ratio of the first product flow rate to the feed flow rate is less than or equal to the first component's fraction of the feed, and the ratio of the second product flow rate to the feed flow rate is less than or equal to the second component's fraction of the feed.

First claim

The invention claimed is:

1. A method for controlling gas separation of a gas mixture comprising a first component and a second component, the method comprising contacting a feed containing the gas mixture with an adsorbent in a bed in a column in a dual reflux swing adsorption process such that a first component of a gas mixture attains or exceeds a desired purity and a second component of the gas mixture attains or exceeds a desired purity, wherein the mathematical product of the cycle feed time and the sum of the molar feed flow rate and the molar reflux flow rate directed to the column does not exceed the maximum number of moles that can be treated per bed per cycle and wherein the ratio of the first product flow rate to the feed flow rate is less than or equal to the first component's fraction of the feed, and the ratio of the second product flow rate to the feed flow rate is less than or equal to the second component's fraction of the feed.

2. A method for controlling gas separation according to claim 1 , wherein the product of the cycle feed time and the sum of the molar flow rates of the feed and reflux directed to the feed column is maintained as close as possible to the maximum number of moles that can be treated per bed per cycle.

3. A method for controlling gas separation according to claim 1 , wherein the product of the cycle feed time and the sum of the molar flow rates of the feed and reflux directed to the feed column is maintained as close as possible to, but without exceeding, the maximum number of moles that can be treated per bed per cycle.

4. A method for controlling gas separation according to claim 1 , wherein the ratios of the product flow rates to the feed flow rates are maintained at the same values as the corresponding fractions of the target components in the feed mixture composition.

5. A method for controlling gas separation according to claim 1 , wherein the reflux flow rate is a sufficiently large fraction of the feed flow rate such that both the enrichment factor for the heavy component and/or the stripping factor for the light component are both not less than the ratio of the bed pressures used in the process.

6. A method for controlling gas separation according to claim 1 , wherein the swing adsorption process is selected from the group of mechanisms that can be used to reverse adsorption, comprising pressure swing, thermal swing, displacement purge or nonadsorbable purge (i.e. partial pressure reduction), or a combination of the above.

7. A method for controlling gas separation according to claim 1 , wherein the gas mixture includes natural gas, coal mining gas, coalbed methane, biogas, ventilation air in coal mines and nitrogen vent gas from LNG plants.

8. A method for controlling gas separation according to claim 1 , wherein mixtures with a methane to nitrogen ratio of about 0.1 or greater are treated to increase the concentration of the methane component.

9. A method for controlling gas separation according to claim 1 , wherein gas streams containing as little as 0.5% methane are purified by the method of the invention down to 100 ppmv methane.

10. A method for controlling gas separation according to claim 1 , wherein the adsorbent has a selectivity for the first component over the second component of greater than one.

11. A method for controlling gas separation according to claim 1 , wherein the adsorbent has an equilibrium selectivity for methane over nitrogen greater than 2.

12. A method for controlling gas separation according to claim 1 , wherein the adsorbent has an equilibrium selectivity for methane over nitrogen greater than 5.

13. A method for controlling gas separation according to claim 1 , wherein the adsorbent is kinetically selective for nitrogen over methane.

14. A method for controlling gas separation according to claim 1 , wherein the adsorbent is selected from the group comprising activated carbons, zeolites and ionic-liquidic zeolites, carbon molecular sieves, clinoptilolite and combinations thereof.

15. A method for controlling gas separation according to claim 1 , wherein the cycle-feed time is shorter than the characteristic sorption time of the slower and less adsorbed gas component but longer than the characteristic sorption time of the faster and more adsorbed gas component.

Assignees

• Univ Western Australia
• Chevron Usa Inc

Inventors

• May Eric Freemantle
• Li Gang
• Chan Kaman Ida
• Huang Stanley Hsing-Wei
• Saleman Thomas Leroy Hinton

Classifications

• C07C7/13

  by molecular-sieve technique · CPC title

• B01D2259/40045

  with two sub-steps · CPC title

• B01D2256/245

  Methane · CPC title

• B01D2253/102

  Carbon · CPC title

• B01D2258/05

  Biogas · CPC title