US4588427A
Expired / Lapsed
US
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Method and apparatus for purification of high N2 content gas
Assignee: Dm International Inc
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Filing: 1985-03-13
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Granted: 1986-05-13
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Expires: 2005-03-13
Abstract
Abstract Nitrogen and methane are separated in a nitrogen-methane cryogenic fractionator operating at a temperature between the boiling points of nitrogen and methane. A distillative aid or absorbent is injected into the nitrogen-methane cryogenic fractionator for enhancing separation, for enabling an increase in operating pressure, and for enabling a high separation rate at relatively high temperature.
Inventors
- 👤 Jame Yao
- 👤 Jong J. Chen
- 👤 Douglas G. Elliot
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 03:36
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/0228; F25J3/0257; F25J3/0204; F25J3/0209; F25J3/0233; F25J3/0238; F25J2200/00; F25J2200/02; F25J2200/04; F25J2200/50; F25J2200/70; F25J2200/74; F25J2200/76; F25J2205/00; F25J2205/02; F25J2205/04; F25J2205/50; F25J2240/00; F25J2240/02; F25J2245/00; F25J2245/02; F25J2270/00; F25J2270/02; F25J2270/88; F25J2290/00; F25J2290/40; Y; Y10; Y10S; Y10S62/00; Y10S62/927
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
209 words
A method for separating nitrogen from methane in a gaseous mixture including nitrogen and methane, comprisng the steps of cooling the gaseous mixture to a temperature below the boiling point of methane but above the boiling point of nitrogen, feeding the cooled mixture to a nitrogen-methane cryogenic fractionator to provide methane condensation, injecting into the fractionator a distillative aid including a liquid material selected from the group consisting of ethane, propane, isobutane, normal butane and mixtures thereof to increase the critical pressure for the mixture sufficient to reduce product recompression costs, to increase the relative volatility of nitrogen to methane, and to aid condensation by absorbing a portion of the methane, passing a bottoms fraction from the nitrogen-methane cryogenic fractionator including a mixture of distillative aid and liquid methane to a regenerator, heating the mixture of distillative aid and liquid methane in the regenerator to form an overhead stream of methane and a bottoms fraction of distillative aid, cooling and returning the bottoms fraction of distillative aid for the above injection into the nitrogen-methane cryogenic fractionator sufficient to provide condensation of methane which results in a reduced circulation rate for the distillative aid, withdrawing methane from the regenerator as product, and withdrawing nitrogen overhead from the nitrogen-methane cryogenic fractionator.
Claim 2
Independent Claim
209 words
A method for separating nitrogen from methane in a gaseous mixture including nitrogen and methane, comprisng the steps of cooling the gaseous mixture to a temperature below the boiling point of methane but above the boiling point of nitrogen, feeding the cooled mixture to a nitrogen-methane cryogenic fractionator to provide methane condensation, injecting into the fractionator a distillative aid including a liquid material selected from the group consisting of ethane, propane, isobutane, normal butane and mixtures thereof to increase the critical pressure for the mixture sufficient to reduce product recompression costs, to increase the relative volatility of nitrogen to methane, and to aid condensation by absorbing a portion of the methane, passing a bottoms fraction from the nitrogen-methane cryogenic fractionator including a mixture of distillative aid and liquid methane to a regenerator, heating the mixture of distillative aid and liquid methane in the regenerator to form an overhead stream of methane and a bottoms fraction of distillative aid, cooling and returning the bottoms fraction of distillative aid for the above injection into the nitrogen-methane cryogenic fractionator sufficient to provide condensation of methane which results in a reduced circulation rate for the distillative aid, withdrawing methane from the regenerator as product, and withdrawing nitrogen overhead from the nitrogen-methane cryogenic fractionator.
Claim 3
Dependent Claim
24 words
A method as claimed in claim 1 wherein the nitrogen-methane cryogenic fractionator operates at a pressure in the range between 27 to 69 bar.
Claim 4
Dependent Claim
72 words
A method as claimed in claim 1 wherein the feeding of the cooled mixture to the nitrogen methane cryogenic fractionator includes feeding the mixture to an intermediate section of the fractionator, and further including condensing methane from the mixture by means of an inter-condenser interposed between an upper and the intermediate sections of the fractionator, and further condensing methane by means of an overhead condenser in the upper section of the fractionator.
Claim 5
Dependent Claim
30 words
A method as claimed in claim 3 wherein the injecting of the distillative aid includes injecting the distillative aid to pass countercurrent to the nitrogen overhead through the overhead condenser.
Claim 6
Dependent Claim
22 words
A method as claimed in claim 3 wherein the inter and overhead condensers are operated at a temperature of about -134° C.
Claim 7
Dependent Claim
49 words
A method as claimed in claim 1 for removing nitrogen from a natural gas mixture wherein there is included the step of removing ethane and heavier hydrocarbon gas material from the natural gas stream prior to feeding the cooled mixture of nitrogen and methane to the nitrogen-methane cryogenic fractionator.
Claim 8
Dependent Claim
84 words
A method as claimed in claim 1 including the steps of compressing and condensing a portion of the methane overhead from the regenerator for use as refrigerant, flashing a first portion of the refrigerant in condenser means within the nitrogen-methane cryogenic fractionator for removing heat of condensation and absorption of methane, partially flashing a second portion of the refrigerant in heat exchanger means to perform the cooling steps, and injecting an unflashed portion of the second portion of refrigerant as reflux into the regenerator.
Claim 9
Independent Claim
189 words
An apparatus for separating nitrogen from methane comprising means for cooling the gaseous mixture of nitrogen and methane to a temperature below the boiling point of methane but above the boiling point of nitrogen, nitrogen-methane cryogenic factionator means for receivng the cooled mixture of nitrogen and methane, condenser means for condensing methane in the fractionator means, means for injecting a distillative aid including a material selected from the group consisting of ethane, propane, isobutane, normal butane and mixtures thereof as a reflux stream into the nitrogen-methane cryogenic fractionator means to increase the critical pressure for the mixture sufficient to reduce product recompression costs, means for withdrawing a mixture of distillative aid and liquid methane from a bottom of the cryogenic nitrogen-methane fractionator means, a regenerator for receiving the withdrawn mixture of distillative aid and liquid methane to heat the mixture to drive off methane as overhead and produce a lean distillative aid bottoms product, and means for cooling and recirculating the lean distillative aid from the regenerator to the nitrogen-methane cryogenic fractionator means for providing condensation of methane which results in a reduced circulation rate for the distillative aid.
Claim 10
Independent Claim
189 words
An apparatus for separating nitrogen from methane comprising means for cooling the gaseous mixture of nitrogen and methane to a temperature below the boiling point of methane but above the boiling point of nitrogen, nitrogen-methane cryogenic factionator means for receivng the cooled mixture of nitrogen and methane, condenser means for condensing methane in the fractionator means, means for injecting a distillative aid including a material selected from the group consisting of ethane, propane, isobutane, normal butane and mixtures thereof as a reflux stream into the nitrogen-methane cryogenic fractionator means to increase the critical pressure for the mixture sufficient to reduce product recompression costs, means for withdrawing a mixture of distillative aid and liquid methane from a bottom of the cryogenic nitrogen-methane fractionator means, a regenerator for receiving the withdrawn mixture of distillative aid and liquid methane to heat the mixture to drive off methane as overhead and produce a lean distillative aid bottoms product, and means for cooling and recirculating the lean distillative aid from the regenerator to the nitrogen-methane cryogenic fractionator means for providing condensation of methane which results in a reduced circulation rate for the distillative aid.
Claim 11
Dependent Claim
46 words
The apparatus of claim 8 wherein the condenser means of the nitrogen-methane cryogenic fractionator means includes an inter-condenser for condensing bulk methane from the feedstream, and an overhead condenser for receiving a flow of regenerated distillative aid and for condensing further methane from the gaseous stream.
Claim 12
Dependent Claim
31 words
The apparatus of claim 9 for separating nitrogen from a natural gas stream including means for separating ethane and heavier hydrocarbons from the cooled mixture prior to the nitrogen-methane cryogenic fractionator.
Claim 13
Dependent Claim
109 words
The apparatus of claim 8 including means for compressing and condensing a portion of the methane overhead from the regenerator into refrigerant, means for flashing a first portion of the refrigerant in the condenser means of the fractionator to remove heat of condensation and absorption of methane, said gaseous mixture cooling means and said distillative aid cooling means including cold box heat exchange means, means for partially flashing a second portion of the refrigerant in the cold box heat exchange means to provide a portion of the cooling duty thereto, and means for injecting an unflashed second portion of the second portion of refrigerant as reflux in the regenerator.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
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| 3.5 Years (Year 4) | 1989-05-12 | 1989-11-11 | 1990-05-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-05-12 | 1993-11-11 | 1994-05-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-05-12 | 1997-11-11 | 1998-05-13 | $7700.00 | Window Closed / Lapsed |