Natural gas enrichment process

• US 5,536,300 A
• Filed: 10/21/1994
• Issued: 07/16/1996
• Est. Priority Date: 10/21/1994
• Status: Expired due to Term

• Current Assignee: IACX Energy, LLC
• Original Assignee: Nitrotec Corporation
• Inventors: Reinhold, Herbert E. III, Knaebel, Kent S., D'Amico, Joseph S.
• Primary Examiner(s): SPITZER, ROBERT H
• Application Number:
  US08/326,916
• Time in Patent Office: 634 Days
• Field of Search: 95/98, 95/100-105, 95/143-147
• US Class Current: 95/101
• CPC Class Codes: B01D 2253/102 Carbon
• CPC Class Codes: B01D 2253/116 Molecular sieves other than zeolites
• CPC Class Codes: B01D 2253/304 Linear dimensions, e.g. particle shape, diameter
• CPC Class Codes: B01D 2256/10 Nitrogen
• CPC Class Codes: B01D 2256/24 Hydrocarbons
• CPC Class Codes: B01D 2257/102 Nitrogen
• CPC Class Codes: B01D 2257/504 Carbon dioxide
• CPC Class Codes: B01D 2257/702 Hydrocarbons
• CPC Class Codes: B01D 2259/40003 Methods relating to valve switching
• CPC Class Codes: B01D 2259/40015 with two sub-steps
• CPC Class Codes: B01D 2259/40032 with three sub-steps
• CPC Class Codes: B01D 2259/403 using three beds
• CPC Class Codes: B01D 53/047 Pressure swing adsorption
• CPC Class Codes: B01D 53/0476 Vacuum pressure swing adsorption
• CPC Class Codes: C10G 5/02 with solid adsorbents
• CPC Class Codes: C10L 3/10 Working-up natural gas or synthetic natural gas
• CPC Class Codes: Y02C 20/40 of CO2

Abstract

A natural gas feed stream containing significant quantities of nitrogen can be increased to a content of greater than 95 percent by volume of natural gas, and preferably greater than about 98 percent, by passing the natural gas feed stream sequentially through at least four adsorbent beds which are cycled through six phases comprising an adsorption phase to adsorb natural gas, a recycle phase to remove feed gas from the voids in the adsorbent bed and nitrogen from the adsorbent by the passage of a depressurization gas therethrough to produce a recycle gas, a depressurization phase to reduce the adsorbent bed pressure to about ambient and to produce the depressurization gas, an evacuation phase where the pressure in the adsorbent is further reduced and an enriched natural gas product stream recovered, a pressurization phase where the pressure in the adsorbent bed is increased using nitrogen gas from a bed in an adsorption phase, and further pressurizing the adsorbent bed in a recycle feed pressurization phase by the flow of the recycle gas therein.

Claims

1. A method for purifying a gas stream containing primarily hydrocarbon gases and nitrogen by flowing said gas stream through a plurality of adsorbent beds each containing an adsorbent which selectively adsorbs said hydrocarbon gases with said nitrogen gas substantially passing therethrough, cycling each of said adsorbent beds sequentially through a series of phases comprising an adsorption phase, a recycle phase, a depressurization phase, an evacuation phase, a nitrogen pressurization phase and a recycle feed pressurization phase, said adsorption phase comprising passing said gas stream into a first adsorbent bed at an elevated pressure for a first part of a first period of time with said hydrocarbon gases being adsorbed therein and collecting a portion of said nitrogen gas substantially passing therethrough for use in pressurizing an adsorbent bed that is to enter said adsorption phase, while said first adsorbent bed is in said adsorption phase depressurizing a third adsorbent bed in said depressurization phase to a first lower pressure to produce a depressurization gas and passing said depressurization gas through a fourth adsorbent bed in said recycle phase and collecting a recycle feed gas therefrom for use at least in further pressurizing an adsorbent bed that is to enter said adsorption phase, and evacuating a second adsorbent bed in said evacuation phase to a lowest pressure and recovering a hydrocarbon gas product containing substantially hydrocarbon gases, said first adsorbent bed prior to undergoing said adsorption phase being repressurized with a portion of said nitrogen gas in said nitrogen pressurization phase and then with a portion of said recycle feed gas in said recycle feed pressurization phase.

2. A method as in claim 1 wherein when said gas stream contains less than about 75 percent by volume hydrocarbons a portion of the hydrocarbon gas product is flowed to the fourth adsorbent bed undergoing said recycle phase.

3. A method as in claim 1 wherein when said gas stream contains more than about 75 percent by volume hydrocarbons a portion of the depressurization gas is flowed to said hydrocarbon gas product.

4. A method as in claim 1 wherein said first adsorbent bed is pressurized by said nitrogen gas and is flowed countercurrent to the flow of said gas stream in said adsorption phase and then a portion of said recycle feed gas is flowed cocurrent with the flow of said gas stream in said adsorption phase to pressurize said first adsorbent bed.

5. A method as in claim 1 wherein each of said recycle phase, said depressurization phase and said evacuation phase are conducted for equivalent periods of time and said nitrogen pressurization phase, said recycle feed pressurization phase and said adsorption phase are collectively conducted for said equivalent period of time.

6. A method as in claim 1 wherein there are at least three adsorbent beds.

7. A method as in claim 1 wherein said adsorbent is a porous activated carbon material that is selective for the adsorption of hydrocarbons.

8. A method is in claim 1 wherein the depressurization gas from said third adsorbent bed contains more than about 90 percent by volume hydrocarbon gases.

9. A method as in claim 1 wherein the hydrocarbon gas product from said second adsorbent bed contains more than about 98 percent by volume hydrocarbon gases.

10. A method as in claim 1 wherein said elevated pressure is a pressure of about 25 to 150 psia.

11. A method for purifying a gas stream containing primarily hydrocarbon gases and nitrogen by flowing said gas stream at an elevated pressure through a plurality of adsorbent beds each containing an adsorbent which selectively adsorbs said hydrocarbon gases with said nitrogen gas substantially passing therethrough, cycling each of said adsorbent beds sequentially through a series of phases comprising an adsorption phase, a recycle phase, a depressurization phase, an evacuation phase, a nitrogen pressurization phase and a recycle feed pressurization phase, said adsorption phase comprising flowing said gas stream at an elevated pressure into an adsorbent bed undergoing said adsorption phase with said hydrocarbon gases being adsorbed in said adsorbent bed and said nitrogen gas substantially passing therethrough;

said recycle phase comprising compressing an effluent depressurization gas from an adsorbent bed undergoing said depressurization phase and flowing said depressurization gas into an adsorbent bed which has completed said adsorption phase and is in said recycle phase with a recycle feed gas flowing therefrom, flowing a portion of said recycle feed gas to an adsorbent bed that is to undergo said adsorption phase to at least partially pressurize said adsorbent bed;

said evacuation phase comprising reducing the pressure in an adsorbent bed that has completed said depressurization phase to less than about ambient pressure and recovering a product gas that contains adsorbed hydrocarbon gases;

said pressurization phase comprising flowing a portion of said nitrogen gas from an adsorbent bed on said adsorption phase into an adsorbent bed on said nitrogen pressurization phase to at least partially pressurize said adsorbent bed, and said recycle feed pressurization phase comprising flowing said recycle feed gas into an adsorbent bed which has completed said nitrogen pressurization phase to additionally pressurize said adsorbent bed.

12. A method as in claim 11 wherein when said gas stream contains more than about 75 percent by volume hydrocarbons a portion of the depressurization gas is flowed to hydrocarbon gas product.

13. A method as in claim 11 wherein when said gas stream contains less than about 75 percent by volume hydrocarbons a portion of the adsorbed hydrocarbon product gas from said evacuation phase is flowed to the adsorbent bed undergoing said recycle phase.

14. A method as in claim 11 wherein in said evacuation phase the gas in an adsorbent bed undergoes a reduction in pressure to more than about 20 inches of Hg vacuum flows in a direction countercurrent to the flow of said gas stream in said adsorption phase.

15. A method as in claim 11 wherein in said recycle phase the gas in an adsorbent bed undergoing the recycle phase flows cocurrent to the flow of said gas stream in said adsorption phase.

16. A method as in claim 11 wherein in the conduct of the phases there are at least three adsorbent beds.

17. A method as in claim 11 wherein said adsorbent is a porous activated carbon that is selective for the adsorption of hydrocarbons.

18. A method as in claim 11 wherein the hydrocarbon gas product from the evacuation phase contains more than about 95 percent by volume hydrocarbon gases.

19. A method as in claim 18 wherein the hydrocarbon gas product from the evacuation phase contains more than about 98 percent by volume hydrocarbon gases.

20. A method as in claim 11 wherein said elevated pressure is about 25 to 150 psia.