US5632803A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Enhanced helium recovery
Assignee: Nitrotec Corp
•
Filing: 1995-08-21
•
Granted: 1997-05-27
•
Expires: 2015-08-21
Abstract
Abstract The disclosed hybrid membrane and pressure swing adsorption process can recover helium from source streams of about 0.5 to 5 percent by volume helium and concentrate the helium to a concentration of greater than about 98 percent by volume. The process comprises a membrane separation followed by two stages of pressure swing adsorption which are used in series. The source gas will primarily contain hydrocarbons but will contain some nitrogen. The membrane unit will contain a semipermeable membrane which is permeably selective for helium and will to the extent feasible reject hydrocarbons. The permeate gas will be increased in helium content by 2 to 10 times. Part of the residue gas is used in the regeneration of the adsorbent beds in the first stage of pressure swing adsorption. Each stage of pressure swing adsorption will contain a plurality of adsorbent beds, and will be cycled through multiple phases. In the first stage the adsorbent beds will sequentially undergo the phases of adsorption, recycle, depressurization, evacuation, helium pressurization and recycle feed pressurization. The product gas from the first stage is flowed to the second stage and in the second stage sequentially will undergo the phases of adsorption, depressurization, evacuation, purge, and helium pressurization. The offgas from the evacuation and purge in the second stage is flowed to input to the first stage. The process efficiently produces a product stream with a helium content of more than 98 percent by volume.
Inventors
- 👤 Glenn Stoner
- 👤 Herbert E. Reingold, III
- 👤 Joseph S. D'Amico
- 👤 Kent S. Knaebel
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 10:24
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01D53/047; B01D53/22; B01D53/229; C; C01; C01B; C01B23/00; C01B23/001; C01B23/0036; C01B23/0052; C01B23/0094; B01D2253/00; B01D2253/10; B01D2253/102; B01D2253/104; B01D2253/106; B01D2253/30; B01D2253/302; B01D2253/304; B01D2256/00; B01D2256/18; B01D2257/00; B01D2257/10; B01D2257/11; B01D2259/00; B01D2259/40; B01D2259/404; B01D2259/406; B01D2259/41; C01B2210/00; C01B2210/0001; C01B2210/0009; C01B2210/001; C01B2210/0014; C01B2210/0029; C01B2210/0031; C01B2210/0043; C01B2210/0068; C01B2210/007
Claims Analysis
Total Claims: 23
Claim 1
Independent Claim
220 words
A method for the separation of helium from an input gas stream containing helium and other gases comprising feeding said input gas from a source to a membrane separation unit at an elevated pressure, flowing a residue stream from said membrane separation unit, a first portion of said residue gas stream being flowed to the source of said input gas and flowing a permeate gas stream enriched in helium from said membrane separation unit to a first stage of a first stage and a second stage pressure swing adsorption unit and after processing said permeate gas in said first stage of pressure swing adsorption flowing the non-adsorbed portion of said permeate gas from said first stage of pressure swing adsorption to said second stage of pressure swing adsorption, said first stage of pressure swing adsorption and said second stage of pressure swing adsorption each containing a plurality of interconnected adsorbent beds, the first stage of pressure swing adsorption concentrating the helium in said input gas stream to greater than about 50 percent helium by volume and in said second stage of pressure swing adsorption concentrating said input gas stream to greater than about 95 percent helium by volume, a second portion of said residue gas stream being fed to said first stage of pressure swing adsorption as a processing gas.
Claim 2
Independent Claim
220 words
A method for the separation of helium from an input gas stream containing helium and other gases comprising feeding said input gas from a source to a membrane separation unit at an elevated pressure, flowing a residue stream from said membrane separation unit, a first portion of said residue gas stream being flowed to the source of said input gas and flowing a permeate gas stream enriched in helium from said membrane separation unit to a first stage of a first stage and a second stage pressure swing adsorption unit and after processing said permeate gas in said first stage of pressure swing adsorption flowing the non-adsorbed portion of said permeate gas from said first stage of pressure swing adsorption to said second stage of pressure swing adsorption, said first stage of pressure swing adsorption and said second stage of pressure swing adsorption each containing a plurality of interconnected adsorbent beds, the first stage of pressure swing adsorption concentrating the helium in said input gas stream to greater than about 50 percent helium by volume and in said second stage of pressure swing adsorption concentrating said input gas stream to greater than about 95 percent helium by volume, a second portion of said residue gas stream being fed to said first stage of pressure swing adsorption as a processing gas.
Claim 3
Dependent Claim
132 words
A method for the separation of helium as in claim 1 wherein in said first stage of pressure swing adsorption there are six phases, each interconnected adsorbent bed undergoing said six phases for each complete cycle, said six phases comprising in sequence an adsorption phase, a recycle phase, a depressurization phase, an evacuation phase, a helium pressurization phase and a recycle feed pressurization phase, said second portion of said residue gas from said membrane separation unit being flowed to an adsorbent bed on said recycle phase with an effluent recycle feed gas enriched in helium flowing therefrom, said recycle feed gas being flowed to an adsorbent bed that is to enter said adsorption phase to pressurize said adsorbent bed to about the operating pressure of said first stage of pressure swing adsorption.
Claim 4
Dependent Claim
225 words
A method for the separation of helium as in claim 2 wherein there are at least four adsorbent beds, feeding said input gas stream to the input end of a first adsorbent bed of said first stage entering on said adsorption phase and selectively adsorbing said other gases, collecting a gas enriched in helium flowing from said first adsorbent bed of said first stage and flowing a portion thereof to said second stage pressure swing adsorption and a portion thereof to a second adsorbent bed of said first stage that has completed said evacuation phase and that has entered said helium pressurization phase, concurrently depressurizing a fourth adsorbent bed of said first stage and producing an effluent gas, flowing said second portion of said residue gas to said first adsorbent bed, upon the completion of said adsorption phase and the initiation of said recycle phase, flowing the effluent from said first adsorbent bed of said first stage during said recycle phase to a second adsorbent bed of said first stage upon the completion of said helium pressurization phase and that is to enter said adsorption phase to pressurize said second adsorbent bed of said first stage to about input gas stream pressure, and concurrently evacuating a third adsorbent bed of said first stage that has completed said depressurization phase to remove said other gases therefrom.
Claim 5
Dependent Claim
55 words
A method for the separation of helium as in claim 3 wherein some of said effluent gas from depressurizing said fourth adsorbent bed and said other gases from said third adsorbent bed which has undergone said evacuation phase are pressurized and flowed for use as an energy source in the operation of said separation method.
Claim 6
Dependent Claim
33 words
A method for the separation of helium as in claim 3 wherein said second adsorbent bed of said first stage is further pressurized with said input gas prior to entering an adsorption phase.
Claim 7
Dependent Claim
157 words
A method for the separation of helium as in claim 2 wherein in said second stage of pressure swing adsorption there are five phases, each interconnected adsorbent bed undergoing said five phases for each complete cycle said five phases comprising in sequence an adsorption phase, a depressurization phase, an evacuation phase, a purge phase and a helium pressurization phase, flowing a feed gas enriched in helium from said first stage to an adsorbent bed in said second stage undergoing said adsorption phase with a further enriched helium gas effluent flowing therefrom, flowing a first portion of said further enriched helium gas to purge other gases from an adsorbent bed in said purge phase, flowing a second portion of said enriched helium gas to an adsorbent bed that has completed said purge phase and which is to enter said adsorption phase to pressurize said adsorbent bed, and flowing a third portion of said further enriched helium to product.
Claim 8
Dependent Claim
251 words
A method for the separation of helium as in claim 6 wherein there are at least four adsorbent beds in said second stage of pressure swing adsorption, feeding said gas from said first stage as a feed gas to a first adsorbent bed in said second stage and collecting a first portion, a second portion and a third portion of a further enriched helium gas therefrom, concurrently depressurizing a fourth adsorbent bed of said second stage which has completed the production of said further enriched helium and which contains substantial amounts of said other gases, recovering an effluent second stage recycle gas from said fourth adsorbent bed of said second stage and pressurizing said second stage recycle gas to about the pressure of said feed gas to said second stage and flowing said second stage recycle gas to said first adsorbent bed of said second stage, concurrently reducing the pressure in a third adsorbent bed of said second stage to less than about ambient pressure and removing a portion of said other gases therefrom, concurrently flowing said first portion of further enriched helium from said first adsorbent bed of said second stage to a third adsorbent bed of said second stage which has completed said evacuation phase as a purge gas and further removing said other gases therefrom, and concurrently flowing said second portion of said further enriched helium to a second adsorbent bed of said second stage to increase the pressure within said second adsorbent bed of said second stage.
Claim 9
Dependent Claim
35 words
A membrane separation unit as in claim 7 wherein at least some of said other gases from said third adsorbent bed of said second stage are fed to the input to said membrane separation unit.
Claim 10
Dependent Claim
38 words
A membrane separation unit as in claim 7 wherein at least some of said other gases from said third adsorbent bed of said second stage are fed to the input to said first stage of pressure swing adsorption.
Claim 11
Dependent Claim
24 words
A method for the separation of helium as in claim 6 wherein the adsorbent within each of said adsorbent beds is an activated carbon.
Claim 12
Dependent Claim
24 words
A method for the separation of helium as in claim 2 wherein the adsorbent within each of said adsorbent beds is an activated carbon.
Claim 13
Dependent Claim
18 words
A method as in claim 1 wherein the source of said input gas is a natural gas pipeline.
Claim 14
Independent Claim
747 words
A method for the separation of helium from an input gas stream containing helium and other gases comprising feeding said input gas from a source to a membrane separation unit at an elevated pressure, flowing a first portion of a residue gas stream from said membrane separation unit to the source of said input gas and flowing a permeate gas stream to a first stage of a first stage and second stage of pressure swing adsorption, each stage containing a plurality of interconnected adsorbent beds, said first stage of pressure swing adsorption concentrating the helium in said gas stream to greater than about 75 percent helium by volume and in said second stage of pressure swing adsorption concentrating said gas stream to greater than about 95 percent helium by volume, at least some of an off gas from the evacuation of an adsorbent bed in said second stage to below about ambient pressure being fed along with said input gas stream to the input of the first stage of pressure swing adsorption, said first stage consisting of at least four interconnected adsorbent beds, each adsorbent bed undergoing six phases for each complete cycle of pressure swing adsorption, said six phases comprising in sequence an adsorption phase, a recycle phase, a depressurization phase, an evacuation phase, a helium pressurization phase and a recycle feed pressurization phase, feeding said input gas stream to the input end of a first adsorbent bed of said first stage entering on said adsorption phase and selectively adsorbing said other gases, collecting a gas enriched in helium flowing from said first adsorbent bed of said first stage and flowing a portion thereof to a second adsorbent bed of said first stage that has completed said evacuation phase and that has entered said helium pressurization phase, concurrently depressurizing a fourth adsorbent bed of said first stage and collecting a first effluent gas, flowing a second portion of said residue gas to said first adsorbent bed of said first stage upon the completion of said adsorption phase and the initiation of said recycle phase, flowing the effluent from said first adsorbent bed of said first stage during said recycle phase to a second adsorbent bed of said first stage upon the completion of said helium pressurization phase and that is to enter said adsorption phase to pressurize said second adsorbent bed of said first stage to about input gas stream pressure, concurrently evacuating a third adsorbent bed of said first stage that has completed said depressurization phase to remove said other gases therefrom and to collect a second effluent gas, flowing another portion of said gas enriched in helium to a second stage of pressure swing adsorption which consists of at least four interconnected adsorbent beds, each such adsorbent bed undergoing five phases for each complete cycle of pressure swing adsorption, said five phases comprising in sequence an adsorption phase, a depressurization phase, an evacuation phase, a purge phase and a helium pressurization phase, feeding said enriched helium gas from said first stage as a feed gas to a first adsorbent bed in said second stage and collecting three portions of a further enriched helium gas therefrom, concurrently depressurizing a fourth adsorbent bed of said second stage which has completed the production of said further enriched helium and which contains substantial amounts of said other gases, depressurizing and recovering an effluent second stage recycle gas from said fourth adsorbent bed of said second stage and pressurizing said second stage recycle gas to about the pressure of said feed gas to said second stage and flowing said second stage recycle gas to said first adsorbent bed of said second stage, concurrently reducing the pressure in a third adsorbent bed of said second stage to less than about ambient pressure and removing a portion of said other gases therefrom, concurrently flowing a first portion of further enriched helium from said first adsorbent bed of said second stage to a third adsorbent bed of said second stage which has completed said evacuation phase as a purge gas and further removing said other gases therefrom, concurrently flowing a second portion of said further enriched helium to a second adsorbent bed of said second stage to increase the pressure within such adsorbent bed, and flowing some of said other gases from said third adsorbent bed of said second stage to at least one of said first adsorbent bed in said first stage and the input gas to said membrane separation unit.
Claim 15
Independent Claim
747 words
A method for the separation of helium from an input gas stream containing helium and other gases comprising feeding said input gas from a source to a membrane separation unit at an elevated pressure, flowing a first portion of a residue gas stream from said membrane separation unit to the source of said input gas and flowing a permeate gas stream to a first stage of a first stage and second stage of pressure swing adsorption, each stage containing a plurality of interconnected adsorbent beds, said first stage of pressure swing adsorption concentrating the helium in said gas stream to greater than about 75 percent helium by volume and in said second stage of pressure swing adsorption concentrating said gas stream to greater than about 95 percent helium by volume, at least some of an off gas from the evacuation of an adsorbent bed in said second stage to below about ambient pressure being fed along with said input gas stream to the input of the first stage of pressure swing adsorption, said first stage consisting of at least four interconnected adsorbent beds, each adsorbent bed undergoing six phases for each complete cycle of pressure swing adsorption, said six phases comprising in sequence an adsorption phase, a recycle phase, a depressurization phase, an evacuation phase, a helium pressurization phase and a recycle feed pressurization phase, feeding said input gas stream to the input end of a first adsorbent bed of said first stage entering on said adsorption phase and selectively adsorbing said other gases, collecting a gas enriched in helium flowing from said first adsorbent bed of said first stage and flowing a portion thereof to a second adsorbent bed of said first stage that has completed said evacuation phase and that has entered said helium pressurization phase, concurrently depressurizing a fourth adsorbent bed of said first stage and collecting a first effluent gas, flowing a second portion of said residue gas to said first adsorbent bed of said first stage upon the completion of said adsorption phase and the initiation of said recycle phase, flowing the effluent from said first adsorbent bed of said first stage during said recycle phase to a second adsorbent bed of said first stage upon the completion of said helium pressurization phase and that is to enter said adsorption phase to pressurize said second adsorbent bed of said first stage to about input gas stream pressure, concurrently evacuating a third adsorbent bed of said first stage that has completed said depressurization phase to remove said other gases therefrom and to collect a second effluent gas, flowing another portion of said gas enriched in helium to a second stage of pressure swing adsorption which consists of at least four interconnected adsorbent beds, each such adsorbent bed undergoing five phases for each complete cycle of pressure swing adsorption, said five phases comprising in sequence an adsorption phase, a depressurization phase, an evacuation phase, a purge phase and a helium pressurization phase, feeding said enriched helium gas from said first stage as a feed gas to a first adsorbent bed in said second stage and collecting three portions of a further enriched helium gas therefrom, concurrently depressurizing a fourth adsorbent bed of said second stage which has completed the production of said further enriched helium and which contains substantial amounts of said other gases, depressurizing and recovering an effluent second stage recycle gas from said fourth adsorbent bed of said second stage and pressurizing said second stage recycle gas to about the pressure of said feed gas to said second stage and flowing said second stage recycle gas to said first adsorbent bed of said second stage, concurrently reducing the pressure in a third adsorbent bed of said second stage to less than about ambient pressure and removing a portion of said other gases therefrom, concurrently flowing a first portion of further enriched helium from said first adsorbent bed of said second stage to a third adsorbent bed of said second stage which has completed said evacuation phase as a purge gas and further removing said other gases therefrom, concurrently flowing a second portion of said further enriched helium to a second adsorbent bed of said second stage to increase the pressure within such adsorbent bed, and flowing some of said other gases from said third adsorbent bed of said second stage to at least one of said first adsorbent bed in said first stage and the input gas to said membrane separation unit.
Claim 16
Dependent Claim
23 words
A method for the separation of helium as in claim 13 wherein the adsorbent in each adsorbent bed is an activated carbon adsorbent.
Claim 17
Dependent Claim
32 words
A method for the separation of helium as in claim 13 wherein said second adsorbent bed of said first stage is further pressurized with input gas prior to entering an adsorption phase.
Claim 18
Independent Claim
88 words
A method for the separation of a component gas from an input gas stream containing said component gas and other gases comprising feeding said input gas from a source to a membrane separation unit at an elevated pressure, flowing a residue gas stream from said membrane separation unit, flowing a permeate gas stream from said membrane separation unit to a pressure swing adsorption separation unit, and flowing a portion of said residue gas to said pressure swing adsorption unit for use in regenerating said pressure swing adsorption unit.
Claim 19
Independent Claim
88 words
A method for the separation of a component gas from an input gas stream containing said component gas and other gases comprising feeding said input gas from a source to a membrane separation unit at an elevated pressure, flowing a residue gas stream from said membrane separation unit, flowing a permeate gas stream from said membrane separation unit to a pressure swing adsorption separation unit, and flowing a portion of said residue gas to said pressure swing adsorption unit for use in regenerating said pressure swing adsorption unit.
Claim 20
Dependent Claim
52 words
A method for the separation of a component gas as in claim 16 wherein there are at least two interconnected stages of pressure swing adsorption, said portion of said residue gas being flowed to said first stage of pressure swing adsorption for use in regenerating said first stage of pressure swing adsorption.
Claim 21
Dependent Claim
68 words
A method for the separation of a component gas as in claim 17 wherein in said second stage of pressure swing adsorption there is produced a gas stream rich in said component gas and a gas stream substantially depleted in said component gas, at least a portion of said gas stream substantially depleted in said component gas flowed to the input gas stream to said membrane separation unit.
Claim 22
Dependent Claim
72 words
A method for the separation of a component gas as in claim 17 wherein in said second stage of pressure swing adsorption there is produced a gas stream rich in said component gas and a gas stream substantially depleted in said component gas, at least a portion of said gas stream substantially depleted in said component gas flowed to the permeate gas for input to said first stage pressure swing adsorption unit.
Claim 23
Dependent Claim
19 words
A method for the separation of a component gas as in claim 16 wherein said component gas is helium.
References Cited (Backward Citations)
US3246449A
Cited
US3250080A
Cited
US3324626A
Cited
US3683589A
Cited
US3636679A
Cited
US3797201A
Cited
US3838553A
Cited
US4077780A
Cited
US4171207A
Cited
EP0071553A1
Cited
US4444572A
Cited
US4581044A
Cited
EP0092695A1
Cited
US4529412A
Cited
US4539020A
Cited
US4675030A
Cited
US4578089A
Cited
US4661125A
Cited
US4717407A
Cited
US4599094A
Cited
US4711645A
Cited
US4689062A
Cited
US4752311A
Cited
US4750925A
Cited
US4687498A
Cited
US4666468A
Cited
US4690695A
Cited
US4732577A
Cited
US4770676A
Cited
US4765804A
Cited
US4701187A
Cited
US4705541A
Cited
US4869894A
Cited
US5089048A
Cited
WO1988009306A1
Cited
US5080694A
Cited
US5064446A
Cited
US4813980A
Cited
US5234472A
Cited
US5112590A
Cited
US4892565A
Cited
US4813977A
Cited
US4790858A
Cited
US4836833A
Cited
US4861361A
Cited
US4863492A
Cited
US4913709A
Cited
US4914218A
Cited
EP0394947A2
Cited
US5004482A
Cited
US5026406A
Cited
US4915711A
Cited
US5507856A
Cited
US5354547A
Cited
US5013334A
Cited
US5171333A
Cited
US5006132A
Cited
JPH0490819A
Cited
US5133785A
Cited
US5156656A
Cited
US5207806A
Cited
US5174796A
Cited
US5226931A
Cited
US5344480A
Cited
US5232473A
Cited
US5224350A
Cited
US5411721A
Cited
US5332424A
Cited
US5382280A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 2000-05-26 | 2000-11-25 | 2001-05-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2004-05-26 | 2004-11-25 | 2005-05-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2008-05-26 | 2008-11-25 | 2009-05-27 | $7700.00 | Window Closed / Lapsed |