US3967938A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the separation of a gaseous mixture consisting of water vapor, hydrocarbons, and air
Assignee: Linde GmbH
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Filing: 1974-07-22
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Granted: 1976-07-06
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Expires: 1994-07-22
Abstract
Abstract In the dispensing of gasoline into a tank used for the storage or transportation of gasoline wherein the gasoline displaces a gaseous mixture of air and gasoline, and said mixture is treated to a recovery step to separate said gasoline from said mixture, there is provided an improvement in the recovery step which comprises cooling said mixture to condense out the gasoline and water from the air thereby purifying the air, and then separating the water from the gasoline. One or two main heat exchangers can be employed depending on whether the system is operated continuously or not. A short regeneration time is made possible by the use of steam which expands the heat exchange tubes sufficiently to remove ice cleanly. An absorber using activated carbon is optionally employed in addition to the removal of the gasoline by cooling.
Inventors
- 👤 Werner Daeschler
- 👤 Hans-Jakob Finkenauer
- 👤 Gerhard Frey
- 👤 Hans Rainer
- 👤 Walter Schramm
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 16:09
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D5/00; B01D5/0033; B01D5/0039; B01D5/0054; B01D5/0078; B01D5/0081; B01D5/0087
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
195 words
A process for the separation of hydrocarbons from a compressed gaseous mixture consisting essentially of air, hydrocarbons and water vapor, said process comprising cooling said gaseous mixture in a heat exchanger cooled by indirect heat exchange relationship with a closed refrigeration cycle, said cooling of said gaseous mixture being conducted in a first stage within said cooled heat exchanger to form a liquid condensate of water and hydrocarbons, and in a second stage in said cooled heat exchanger to freeze out residual hydrocarbons and water to form solid deposits on the tube surfaces of the heat exchanger; removing the air freed of water and hydrocarbon from said cooled heat exchanger, said cooled heat exchanger being a regenerated heat exchanger (220) of two alternating heat exchangers (218, 220), said gaseous mixture to be treated, prior to being cooled in the regenerated heat exchanger (220) having been utilized for the regeneration of the other heat exchanger (218) loaded in an earlier switching phase to melt off frozen-out water and hydrocarbons; recovering resultant melted condensate of water and hydrocarbons and the liquid condensate from said first stage, and separating water from resultant liquid phases to recover said hydrocarbons.
Claim 2
Dependent Claim
195 words
A process for the separation of hydrocarbons from a compressed gaseous mixture consisting essentially of air, hydrocarbons and water vapor, said process comprising cooling said gaseous mixture in a heat exchanger cooled by indirect heat exchange relationship with a closed refrigeration cycle, said cooling of said gaseous mixture being conducted in a first stage within said cooled heat exchanger to form a liquid condensate of water and hydrocarbons, and in a second stage in said cooled heat exchanger to freeze out residual hydrocarbons and water to form solid deposits on the tube surfaces of the heat exchanger; removing the air freed of water and hydrocarbon from said cooled heat exchanger, said cooled heat exchanger being a regenerated heat exchanger (220) of two alternating heat exchangers (218, 220), said gaseous mixture to be treated, prior to being cooled in the regenerated heat exchanger (220) having been utilized for the regeneration of the other heat exchanger (218) loaded in an earlier switching phase to melt off frozen-out water and hydrocarbons; recovering resultant melted condensate of water and hydrocarbons and the liquid condensate from said first stage, and separating water from resultant liquid phases to recover said hydrocarbons.
Claim 3
Dependent Claim
42 words
A process according to claim 1, characterized in that the condensates produced during the regeneration of the loaded heat exchanger (218) and/or during the cooling of the gaseous mixture in the regenerated heat exchanger (220) are fed to a common separator (219).
Claim 4
Dependent Claim
32 words
A process according to claim 1, characterized in that gas extensively freed of hydrocarbons after flowing through the regenerated heat exchanger, is expanded (223) and warmed countercurrently with the gaseous mixture (224).
Claim 5
Dependent Claim
11 words
A process according to claim 1 wherein said hydrocarbons are gasoline.
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) | 1979-07-06 | 1980-01-05 | 1980-07-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-07-06 | 1984-01-05 | 1984-07-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-07-06 | 1988-01-05 | 1988-07-06 | $7700.00 | Window Closed / Lapsed |