Patent US4339547A successfully refreshed from Google Patents.
US4339547A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Production of synthetic hydrocarbons from air, water and low cost electrical power
Assignee: Grumman Corp
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Filing: 1980-07-09
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Granted: 1982-07-13
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Expires: 2000-07-09
Abstract
Abstract A process for manufacturing synthetic hydrocarbons such as gasoline and/or kerosene from the synthesis of carbon dioxide and hydrogen. The carbon dioxide is obtained from the atmosphere while the hydrogen is obtained during the electrolysis of water. An intermediate fuel, namely methyl alcohol may be stored for use or upgraded to higher heating value hydrocarbons by a catalytic conversion.
Inventors
- 👤 Marshall J. Corbett
- 👤 Salvatore C. Salina
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 10:08
CPC Classifications
C; C10; C10G; C10G3/00; C10G3/42; C10G3/44; C10G3/48; C10G3/49; C01; C01B; C01B32/00; C01B32/50; C07; C07C; C07C29/00; C07C29/15; C10G2300/00; C10G2300/10; C10G2300/1022; C10G2400/00; C10G2400/02; Y; Y02; Y02P; Y02P30/00; Y02P30/20
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
139 words
A process for manufacturing synthetic hydrocarbons fuels from the synthesis of CO 2 and H 2 , the process comprising the steps: subjecting a NaOH solution to CO 2 present in air, resulting in production of Na 2 CO 3 and NaHCO 3 ; reacting the resulting solution with Cl 2 (a) causing stripping of the CO 2 and (b) forming brine and NaOCl; separating the oxygen from the NaOCl whereby additional brine results; electrolyzing the brine to form H 2 , Cl 2 and NaOH; recycling the resulting Cl 2 for further stripping of CO 2 ; recycling the resulting NaOH for further reaction with CO 2 ; reacting the stripped CO 2 and the H 2 from the electrolyzed brine to form methanol and water; and separating the methanol and water thus permitting collection of the methanol.
Claim 2
Dependent Claim
139 words
A process for manufacturing synthetic hydrocarbons fuels from the synthesis of CO 2 and H 2 , the process comprising the steps: subjecting a NaOH solution to CO 2 present in air, resulting in production of Na 2 CO 3 and NaHCO 3 ; reacting the resulting solution with Cl 2 (a) causing stripping of the CO 2 and (b) forming brine and NaOCl; separating the oxygen from the NaOCl whereby additional brine results; electrolyzing the brine to form H 2 , Cl 2 and NaOH; recycling the resulting Cl 2 for further stripping of CO 2 ; recycling the resulting NaOH for further reaction with CO 2 ; reacting the stripped CO 2 and the H 2 from the electrolyzed brine to form methanol and water; and separating the methanol and water thus permitting collection of the methanol.
Claim 3
Dependent Claim
19 words
The method set forth in claim 1 together with the step of synthesizing hydrocarbon fuel from the separated methanol.
Claim 4
Dependent Claim
39 words
The method set forth in claim 1 together with the step of recycling the water, separated from the methanol, for electrolysis which produces H 2 which is itself recycled for reaction with stripped CO 2 to form the methanol.
Claim 5
Dependent Claim
39 words
The method set forth in claim 2 together with the step of recycling the water, separated from the methanol, for electrolysis which produces H 2 which is itself recycled for reaction with stripped CO 2 to form the methanol.
Claim 6
Dependent Claim
27 words
The method set forth in claim 4 wherein the step of subjecting a NaOH solution to CO 2 occurs during the passage of solution droplets through air.
Claim 7
Dependent Claim
34 words
The method set forth in claim 4 together with the step of transferring exothermic heat, derived from the methanol and hydrocarbon producing steps, to the NaOCl for accelerating the separation of O 2 therefrom.
Claim 8
Dependent Claim
33 words
The method set forth in claim 5 together with the step of transferring exothermic heat, derived from the methanol and hydrocarbon producing steps, for preheating the NaOH solution thereby preventing it from freezing.
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) | 1985-07-12 | 1986-01-11 | 1986-07-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-07-12 | 1990-01-11 | 1990-07-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-07-12 | 1994-01-11 | 1994-07-13 | $7700.00 | Window Closed / Lapsed |