US4066423A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Adsorption-absorption vapor recovery system
Assignee: H-T Management Co
•
Filing: 1976-09-27
•
Granted: 1978-01-03
•
Expires: 1996-09-27
Abstract
Abstract A process for the recovery of light mixed hydrocarbon vapors from an air-hydrocarbon mixture expelled as a result of storage breathing or loading of a vented hydrocarbon vessel. The hydrocarbon vapor components are adsorbed from the mixture, thus permitting venting of the substantially hydrocarbon free air safely to the atmosphere without pollution. The adsorbed hydrocarbons are removed by subjecting the adsorbent bed to a lower pressure, and the hydrocarbon components in the resulting desorption stream are substantially adsorbed for recovery, and the remaining gases from the absorption vessel are passed through a second adsorption bed to substantially remove any hydrocarbons therein.
Inventors
- 👤 James C. McGill
- 👤 William N. Scott
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 21:34
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; C; C07; C07C; C07C7/00; C07C7/005; B01D2256/00; B01D2256/24; B01D2257/00; B01D2257/70; B01D2257/702; B01D2259/00; B01D2259/40; B01D2259/40083; B01D2259/402
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
200 words
A process for recovering light hydrocarbon from an air-hydrocarbon mixture, comprising: passing the air-hydrocarbon mixture through a solid adsorbent bed operated at slightly above atmospheric pressure, capable of selectively adsorbing hydrocarbon components from the mixture to leave substantially hydrocarbon free air; venting the substantially hydrocarbon free air to the atmosphere; lowering the pressure of the hydrocarbon laden solid adsorbent bed by vacuum pumping to desorb the air-hydrocarbon components therefrom and produce a rich air-hydrocarbon mixture; cooling the rich air-hydrocarbon mixture to near ambient temperature; absorbing substantially all of the hydrocarbon components from the rich air-hydrocarbon mixture with a liquid hydrocarbon absorbent in an absorber operating with a sufficiently high L/V ratio to produce a constant composition absorber overhead gas containing hydrocarbon and a recovered liquid hydrocarbon, mixed with said absorbent; recycling the absorber overhead gas from the absorption step to a second solid adsorbent bed, capable of selectively adsorbing the hydrocarbon contained in said absorber overhead gas to leave a substantially hydrocarbon free recycle air; venting the substantially free hydrocarbon recycle air to the atmosphere; cooling a portion of the recovered liquid hydrocarbon; and recycling the cooled recovered hydrocarbon liquid for use as liquid hydrocarbon absorbent in the absorption step.
Claim 2
Dependent Claim
200 words
A process for recovering light hydrocarbon from an air-hydrocarbon mixture, comprising: passing the air-hydrocarbon mixture through a solid adsorbent bed operated at slightly above atmospheric pressure, capable of selectively adsorbing hydrocarbon components from the mixture to leave substantially hydrocarbon free air; venting the substantially hydrocarbon free air to the atmosphere; lowering the pressure of the hydrocarbon laden solid adsorbent bed by vacuum pumping to desorb the air-hydrocarbon components therefrom and produce a rich air-hydrocarbon mixture; cooling the rich air-hydrocarbon mixture to near ambient temperature; absorbing substantially all of the hydrocarbon components from the rich air-hydrocarbon mixture with a liquid hydrocarbon absorbent in an absorber operating with a sufficiently high L/V ratio to produce a constant composition absorber overhead gas containing hydrocarbon and a recovered liquid hydrocarbon, mixed with said absorbent; recycling the absorber overhead gas from the absorption step to a second solid adsorbent bed, capable of selectively adsorbing the hydrocarbon contained in said absorber overhead gas to leave a substantially hydrocarbon free recycle air; venting the substantially free hydrocarbon recycle air to the atmosphere; cooling a portion of the recovered liquid hydrocarbon; and recycling the cooled recovered hydrocarbon liquid for use as liquid hydrocarbon absorbent in the absorption step.
Claim 3
Dependent Claim
241 words
A process for recovering hydrocarbon from an air-hydrocarbon mixture, comprising: passing the air-hydrocarbon mixture through a solid adsorbent bed at slightly above atmospheric pressure, which bed is capable of selectively adsorbing the hydrocarbon components from the mixture to leave substantially hydrocarbon free air; venting the substantially hydrocarbon free air to the atmosphere; subjecting the hydrocarbon laden solid adsorbent bed to a near vacuum with a liquid ring vacuum pump to desorb the hydrocarbon components therefrom and produce a rich air-hydrocarbon vapor mixture containing a liquid from the liquid ring vacuum pump and a recovered liquid hydrocarbon; separating the liquid from the liquid ring vacuum pump and the recovered liquid hydrocarbon from the rich air-hydrocarbon vapor mixture; absorbing substantially all of the hydrocarbon components from the rich air-hydrocarbon vapor mixture with recovered liquid hydrocarbon absorbent in an absorber operating with a sufficiently high L/V ratio to produce a constant composition absorber overhead gas and a recovered liquid hydrocarbon mixed with said absorbent; recycling the absorber overhead gas from the absorption step to a second solid adsorbent bed, capable of selectively absorbing the hydrocarbon therein to leave a substantially free hydrocarbon recycle air; venting the substantially free hydrocarbon recycle air to the atmosphere; separating the liquid ring vacuum pump liquid from the recovered liquid hydrocarbon produced in the separation step; cooling the liquid ring vacuum pump liquid; and recycling said liquid ring vacuum pump liquid for use in the liquid ring vacuum pump.
Claim 4
Dependent Claim
241 words
A process for recovering hydrocarbon from an air-hydrocarbon mixture, comprising: passing the air-hydrocarbon mixture through a solid adsorbent bed at slightly above atmospheric pressure, which bed is capable of selectively adsorbing the hydrocarbon components from the mixture to leave substantially hydrocarbon free air; venting the substantially hydrocarbon free air to the atmosphere; subjecting the hydrocarbon laden solid adsorbent bed to a near vacuum with a liquid ring vacuum pump to desorb the hydrocarbon components therefrom and produce a rich air-hydrocarbon vapor mixture containing a liquid from the liquid ring vacuum pump and a recovered liquid hydrocarbon; separating the liquid from the liquid ring vacuum pump and the recovered liquid hydrocarbon from the rich air-hydrocarbon vapor mixture; absorbing substantially all of the hydrocarbon components from the rich air-hydrocarbon vapor mixture with recovered liquid hydrocarbon absorbent in an absorber operating with a sufficiently high L/V ratio to produce a constant composition absorber overhead gas and a recovered liquid hydrocarbon mixed with said absorbent; recycling the absorber overhead gas from the absorption step to a second solid adsorbent bed, capable of selectively absorbing the hydrocarbon therein to leave a substantially free hydrocarbon recycle air; venting the substantially free hydrocarbon recycle air to the atmosphere; separating the liquid ring vacuum pump liquid from the recovered liquid hydrocarbon produced in the separation step; cooling the liquid ring vacuum pump liquid; and recycling said liquid ring vacuum pump liquid for use in the liquid ring vacuum pump.
Claim 5
Dependent Claim
34 words
A process, as recited in claim 2, the further steps comprising: cooling a portion of the recovered liquid hydrocarbon; and recycling the cooled recovered liquid hydrocarbon for use as absorbent in the absorption step.
Claim 6
Dependent Claim
16 words
A process, as recited in claim 3, wherein the liquid ring vacuum pump liquid is water.
Claim 7
Dependent Claim
21 words
A process, as recited in claim 3, wherein the liquid ring vacuum pump liquid is water mixed with an anti-freeze material.
References Cited (Backward Citations)
US3648436A
Cited
US3771317A
Cited
US3770622A
Cited
US3714790A
Cited
US3947258A
Cited
US3867111A
Cited
US3972201A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-01-02 | 1981-07-04 | 1982-01-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-01-02 | 1985-07-04 | 1986-01-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-01-02 | 1989-07-04 | 1990-01-03 | $7700.00 | Window Closed / Lapsed |