Patent US3092667A successfully refreshed from Google Patents.
US3092667A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the recovery of methanol
Assignee: Gulf Research and Development Co
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Filing: 1959-10-09
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Granted: 1963-06-04
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Expires: 1979-10-09
Abstract
No abstract record available.
Inventors
- 👤 Clarence R Murphy
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 08:44
CPC Classifications
C; C07; C07C; C07C29/00; C07C29/132; C07C29/136; C07C29/14; C07C29/141; C07C29/74; C07C29/88; C07C29/90; C07C45/00; C07C45/27; C07C45/32; C07C45/33
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
205 words
A PROCESS FOR OBTAINING METHANOL WHICH COMPRISES OXIDIZING A GAS SELECTED FROM THE GROUP CONSISTING OF ETHANE, PROPANE AND BUTANE WITH A GAS CONTAINING MOLECULAR OXYGEN AT A TEMPERATURE OF ABOUT 700* TO ABOUT 900* F., TO OBTAIN AN OXYGENATED MIXTURE CONTAINING ESSENTIALLY FORMALDEHYDE, ACETALDEHYDE, METHANOL, HIGHER ALCOHOLS, ACETONE, ACETALS AND ETHYLENE AND PROPYLENE OXIDES, REMOVING FORMALDEHYDE BY EXTRACTION WITH WATER AND A PORTION OF THE ACETALDEHYDE BY FRACTIONATION FFROM THE OXYGENATED MIXTURE AND OBTAINING AN OXYGENATED PRODUCT CONTAINING IN EXCESS OF ABOUT FIVE PERCENT BY WEIGHT THEREOF OF CARBONYL-CONTAINING COMPOUNDS CONSISTING OF ACETALDEHYDE, ACETONE AND ACETALS, DIRECTLY SUBJECTING SAID LATTER OXYGENATED PRODUCT TO HYDROGENATION WITH HYDROGEN IN THE PESENCE OF A HYDROGENATION CATALYST AT A TEMPERATURE OF ABOUT 300* TO ABOUT 350*F. TO OBTAIN A HYDROGENATION PRODUCT CONTAINING FROM ABOUT ONE TO ABOUT THREE PERCENT BY WEIGHT OF CARBONYL-CONTAINING COMPOUNDS, DISTILLING FROM SAID HYDROGENATION PRODUCT AT A TEMPERATURE OF ABOUT 160* TO ABOUT 170*F. A PRODUCT CONSISTING ESSENTIALLY OF METHANOL AND CARBONYL-CONTAINING COMPOUNDS, EXTRACTING SAID METHANOL PRODUCT WITH WATER CONTAINING A BASIC REAGENT SELCTED FROM THE GROUP CONSISTING OF SODIUM HYDROXIDE, POTASSIUM HYDROXIDE AND CALCIUM HYDROXUDE AND THEREAFTER RECOVERING BY DISTILLATION AT A TEMPERATURE OF ABOUT 147* TO ABOUT 150*F. METHANOL FROM SAID EXTRACT.
Claim 2
Dependent Claim
205 words
A PROCESS FOR OBTAINING METHANOL WHICH COMPRISES OXIDIZING A GAS SELECTED FROM THE GROUP CONSISTING OF ETHANE, PROPANE AND BUTANE WITH A GAS CONTAINING MOLECULAR OXYGEN AT A TEMPERATURE OF ABOUT 700* TO ABOUT 900* F., TO OBTAIN AN OXYGENATED MIXTURE CONTAINING ESSENTIALLY FORMALDEHYDE, ACETALDEHYDE, METHANOL, HIGHER ALCOHOLS, ACETONE, ACETALS AND ETHYLENE AND PROPYLENE OXIDES, REMOVING FORMALDEHYDE BY EXTRACTION WITH WATER AND A PORTION OF THE ACETALDEHYDE BY FRACTIONATION FFROM THE OXYGENATED MIXTURE AND OBTAINING AN OXYGENATED PRODUCT CONTAINING IN EXCESS OF ABOUT FIVE PERCENT BY WEIGHT THEREOF OF CARBONYL-CONTAINING COMPOUNDS CONSISTING OF ACETALDEHYDE, ACETONE AND ACETALS, DIRECTLY SUBJECTING SAID LATTER OXYGENATED PRODUCT TO HYDROGENATION WITH HYDROGEN IN THE PESENCE OF A HYDROGENATION CATALYST AT A TEMPERATURE OF ABOUT 300* TO ABOUT 350*F. TO OBTAIN A HYDROGENATION PRODUCT CONTAINING FROM ABOUT ONE TO ABOUT THREE PERCENT BY WEIGHT OF CARBONYL-CONTAINING COMPOUNDS, DISTILLING FROM SAID HYDROGENATION PRODUCT AT A TEMPERATURE OF ABOUT 160* TO ABOUT 170*F. A PRODUCT CONSISTING ESSENTIALLY OF METHANOL AND CARBONYL-CONTAINING COMPOUNDS, EXTRACTING SAID METHANOL PRODUCT WITH WATER CONTAINING A BASIC REAGENT SELCTED FROM THE GROUP CONSISTING OF SODIUM HYDROXIDE, POTASSIUM HYDROXIDE AND CALCIUM HYDROXUDE AND THEREAFTER RECOVERING BY DISTILLATION AT A TEMPERATURE OF ABOUT 147* TO ABOUT 150*F. METHANOL FROM SAID EXTRACT.
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) | 1966-06-03 | 1966-12-03 | 1967-06-04 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1970-06-03 | 1970-12-03 | 1971-06-04 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1974-06-03 | 1974-12-03 | 1975-06-04 | $7700.00 | Window Closed / Lapsed |