US4110091A
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: 1976-03-18
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Granted: 1978-08-29
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Expires: 1996-03-18
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.
Inventors
- 👤 Werner Daeschler
- 👤 Hans Rainer
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 08:41
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: 7
Claim 1
Independent Claim
165 words
A process for the separation of components having a higher boiling point than air from a gaseous mixture consisting essentially of air, hydrocarbons and water vapor, comprising the steps of: (a) passing said gaseous mixture to a heat exchanger provided with cooling tubes containing refrigerant cooled by a closed refrigeration cycle, said cooling of said gaseous mixture being conducted in a first stage within said heat exchanger to form a liquid condensate of water and hydrocarbons, and in a second stage within said heat exchanger to freeze out residual hydrocarbons and water to form solid deposits on the cooling tube surfaces; (b) withdrawing cold, extensively purified air from the heat exchanger proximate the coldest zone thereof; (c) recycling said cold, extensively purified air to said heat exchanger in a separate tube provided therein to cool, by indirect heat exchange, the entering gaseous mixture and warm said cold, extensively purified air; (d) recovering the condensate water and hydrocarbons, and separating water therefrom to recover said hydrocarbons.
Claim 2
Dependent Claim
165 words
A process for the separation of components having a higher boiling point than air from a gaseous mixture consisting essentially of air, hydrocarbons and water vapor, comprising the steps of: (a) passing said gaseous mixture to a heat exchanger provided with cooling tubes containing refrigerant cooled by a closed refrigeration cycle, said cooling of said gaseous mixture being conducted in a first stage within said heat exchanger to form a liquid condensate of water and hydrocarbons, and in a second stage within said heat exchanger to freeze out residual hydrocarbons and water to form solid deposits on the cooling tube surfaces; (b) withdrawing cold, extensively purified air from the heat exchanger proximate the coldest zone thereof; (c) recycling said cold, extensively purified air to said heat exchanger in a separate tube provided therein to cool, by indirect heat exchange, the entering gaseous mixture and warm said cold, extensively purified air; (d) recovering the condensate water and hydrocarbons, and separating water therefrom to recover said hydrocarbons.
Claim 3
Dependent Claim
39 words
A process according to claim 1, wherein the cold extensively purified air if withdrawn in step (b) at a temperature of about -55° C., and is then warmed in said separate tube in the heat exchanger to 10° C.
Claim 4
Dependent Claim
65 words
A process according to claim 1, wherein said gaseous mixture is compressed in a blower prior to step (a), and said heat exchanger is regenerated during time periods wherein no gaseous mixture is being fed to said heat exchanger, said heat exchanger being regenerated by compressing warm air in said blower to a slight superatmospheric pressure and passing said warm air through said heat exchanger.
Claim 5
Dependent Claim
26 words
A process according to claim 1, characterized in that said heat exchanger is regenerated during time periods wherein no gaseous mixture is being fed heat exchanger.
Claim 6
Dependent Claim
26 words
A process according to claim 1 characterized in that the loading of the heat exchanger takes place during the day and the regulation during the night.
Claim 7
Dependent Claim
25 words
A process according to claim 1 characterized in that the heat exchanger is regenerated by blowing thereinto warm air brought to a slight superatmospheric pressure.
References Cited (Backward Citations)
US3115017A
Cited
US3791422A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-08-28 | 1982-02-27 | 1982-08-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-08-28 | 1986-02-27 | 1986-08-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-08-28 | 1990-02-27 | 1990-08-29 | $7700.00 | Window Closed / Lapsed |