US4273566A
Expired / Lapsed
US
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Method and system for the fractionation of ethane-propane mixtures
Assignee: Cabot Corp
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Filing: 1979-06-04
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Granted: 1981-06-16
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Expires: 1999-06-04
Abstract
Abstract Relatively high pressure mixtures consisting essentially of a major ethane component and a minor, but substantial, propane component are separated into relatively pure ethane and propane fractions by subjecting such mixtures to a number of specific cooling steps and an expansion step preparatory to and in combination with a fractional distillation step. The overhead ethane fraction of the method has a propane content of no greater than about 10 mole percent and is provided in the gas phase. The propane bottom fraction of the method is provided in the liquid phase.
Inventors
- 👤 Brian L. Schwarz
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 19:56
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/0228; F25J3/0242; C; C07; C07C; C07C7/00; C07C7/04; F25J3/0204; F25J3/0209; F25J3/0238; F25J2200/00; F25J2200/40; F25J2215/00; F25J2215/62; F25J2215/64
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
298 words
A method for the fractionation of ethane-propane mixtures which comprises the steps of: (a) providing a relatively high pressure entirely liquid feed mixture consisting essentially of between 85 and 70 mole percent ethane and between 15 and 30 mole percent propane: (b) dividing said liquid feed mixture into first and second feed mixture streams; (c) cooling and reducing the pressure of said liquid feed mixture to a temperature sufficiently low to supply all of the refrigeration in the fractionation step of (d), below, and to a relatively low pressure whereat said mixture is maintained in an at least predominantly liquid state, thereby to provide all of the liquid for refluxing purpose in said fractionation step of (d), said first stream being precooled by heat exchange thereof with cold gaseous ethane fraction removed as overhead product from the fractionation tower of step (d), said second stream being precooled by heat exchange thereof with cold distilling liquid removed from the fractionation tower of step (d), said distilling liquid being recycled to the fractionation tower after warming and at least partial vaporization thereof by said second stream to thereby provide reboil heat to said tower, said cooling and pressure reduction being at least partially achieved by expansion cooling of said liquid feed mixture substantially immediately preceding said step (d); (d) introducing the cooled pressure-reduced and at least predominantly liquid feed mixture of (c) into a fractionation tower wherein fractionation of the ethane component from said mixture is achieved at relatively low pressure; (e) removing as overhead product from said fractionation tower, and without reflux condensation thereof, a cold gaseous ethane fraction having a propane content of no greater than about 10 mole percent; and (f) removing as bottom product from said fractionation tower a liquid propane fraction having reduced ethane content.
Claim 2
Independent Claim
298 words
A method for the fractionation of ethane-propane mixtures which comprises the steps of: (a) providing a relatively high pressure entirely liquid feed mixture consisting essentially of between 85 and 70 mole percent ethane and between 15 and 30 mole percent propane: (b) dividing said liquid feed mixture into first and second feed mixture streams; (c) cooling and reducing the pressure of said liquid feed mixture to a temperature sufficiently low to supply all of the refrigeration in the fractionation step of (d), below, and to a relatively low pressure whereat said mixture is maintained in an at least predominantly liquid state, thereby to provide all of the liquid for refluxing purpose in said fractionation step of (d), said first stream being precooled by heat exchange thereof with cold gaseous ethane fraction removed as overhead product from the fractionation tower of step (d), said second stream being precooled by heat exchange thereof with cold distilling liquid removed from the fractionation tower of step (d), said distilling liquid being recycled to the fractionation tower after warming and at least partial vaporization thereof by said second stream to thereby provide reboil heat to said tower, said cooling and pressure reduction being at least partially achieved by expansion cooling of said liquid feed mixture substantially immediately preceding said step (d); (d) introducing the cooled pressure-reduced and at least predominantly liquid feed mixture of (c) into a fractionation tower wherein fractionation of the ethane component from said mixture is achieved at relatively low pressure; (e) removing as overhead product from said fractionation tower, and without reflux condensation thereof, a cold gaseous ethane fraction having a propane content of no greater than about 10 mole percent; and (f) removing as bottom product from said fractionation tower a liquid propane fraction having reduced ethane content.
Claim 3
Dependent Claim
22 words
The method of claim 1 wherein said relatively high pressure feed mixture of (a) has a pressure of at least 450 p.s.i.g.
Claim 4
Dependent Claim
27 words
The method of claim 1 wherein said feed mixture consists essentially of between 80 and 75 mole percent ethane and between 20 and 25 mole percent propane.
Claim 5
Dependent Claim
25 words
The method of claim 1 wherein the precooled first and second feed mixture streams are recombined into a single stream prior to expansion cooling thereof.
Claim 6
Dependent Claim
53 words
The method of claim 1 wherein a portion of the liquid propane fraction contained in the bottom of the fractionation tower is removed therefrom, warmed and at least partially vaporized by heat exchange with a fluid and recycled into the bottom portion of the tower, thereby to provide reboil heat to the tower.
Claim 7
Dependent Claim
39 words
The method of claim 5 wherein said fluid is an at least partially gaseous relatively high pressure feed mixture stream whereby said stream is cooled to entire liquifaction thereof while said portion of said liquid propane fraction is warmed.
Claim 8
Dependent Claim
25 words
The method of claim 1 wherein said gaseous overhead ethane fraction is introduced into a natural gas pipeline transmission system as an adjunctive fuel therefor.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-06-15 | 1984-12-15 | 1985-06-16 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-06-15 | 1988-12-15 | 1989-06-16 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-06-15 | 1992-12-15 | 1993-06-16 | $7700.00 | Window Closed / Lapsed |