US2645599A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for separating wax from wax-oil mixtures
Assignee: ExxonMobil Oil Corp
•
Filing: 1950-11-28
•
Granted: 1953-07-14
•
Expires: 1970-11-28
Abstract
No abstract record available.
Inventors
- 👤 John W Payne
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 16:00
CPC Classifications
C; C10; C10G; C10G73/00; C10G73/02; C10G73/06
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
204 words
A PROCESS FOR SEPARATING WAX AND OIL FROM A WAX-OIL MIXTURE, WHICH COMPRISES ADDING AN AQUEOUS SOLUTION WHICH IS CAPABLE OF REMAINING IN SUBSTANTIALLY THE LIQUID STATE AT THE DEWAXING TEMPERATURE, TO SAID WAX-OIL MIXTURE, IN AN AMOUNT VARYING BETWEEN ABOUT ONE PER CENT AND ABOUT 200 PER CENT, BASED ON THE WEIGHT OF THE WAX-OIL MIXTURE, TO PRODUCE AN AQUEOUS SOLUTION-WAX-OIL MIXTURE; TREATING SAID AQUEOUS SOLUTION-WAX-OIL MIXTURE IN THE PRESENCE OF A SURFACE ACTIVE AGENT THAT PRODUCES A FINITE THREEPHASE CONTACT ANGLE IN THE BUBBLE MACHINE TEST AT THE DEWAXING TEMPERATURE, IN AMOUNTS OF AT LEAST ABOUT 0.01 PER CENT, BASED ON THE WEIGHT OF THE WAX-OIL MIXTURE, BUT LESS THAN THE AMOUNT NECESSARY TO PROMOTE FORMATIONOF A WAX-OIL MIXTURE-IN-AQUEOUS SOLUTION EMULSION IN WHICH THE AQUEOUS SOLUTION IS THE CONTINUOUS PHASE, TO PRODUCE A DISPERSION IN WHICH THE AQUEOUS SOLUTION IS THE DISPERSED PHASE AND THE WAX-OIL MIXTURE IS THE CONTINUOUS PHASE; INTRODUCING A LIQUIFIED, LOW-BOILING MATERIAL INTO SAID DISPERSION; PERMITTING SAID LIQUIFIED, LOW-BOILING MATERIAL TO VAPORIZE TO PRECIPITATE WAX AND TO PRODUCE GAS; CONTINUING SAID TREATING TO ASSOCIATE SAID WAX AND SAID GAS WITH THE DISPERSED AQUEOUS SOLUTION PHASE, THEREBY PRODUCING A WAX-BEARING FROTH; AND SEPARATING SAID WAX-BEARING FROTH FROM SAID DISPERSION.
Claim 2
Dependent Claim
204 words
A PROCESS FOR SEPARATING WAX AND OIL FROM A WAX-OIL MIXTURE, WHICH COMPRISES ADDING AN AQUEOUS SOLUTION WHICH IS CAPABLE OF REMAINING IN SUBSTANTIALLY THE LIQUID STATE AT THE DEWAXING TEMPERATURE, TO SAID WAX-OIL MIXTURE, IN AN AMOUNT VARYING BETWEEN ABOUT ONE PER CENT AND ABOUT 200 PER CENT, BASED ON THE WEIGHT OF THE WAX-OIL MIXTURE, TO PRODUCE AN AQUEOUS SOLUTION-WAX-OIL MIXTURE; TREATING SAID AQUEOUS SOLUTION-WAX-OIL MIXTURE IN THE PRESENCE OF A SURFACE ACTIVE AGENT THAT PRODUCES A FINITE THREEPHASE CONTACT ANGLE IN THE BUBBLE MACHINE TEST AT THE DEWAXING TEMPERATURE, IN AMOUNTS OF AT LEAST ABOUT 0.01 PER CENT, BASED ON THE WEIGHT OF THE WAX-OIL MIXTURE, BUT LESS THAN THE AMOUNT NECESSARY TO PROMOTE FORMATIONOF A WAX-OIL MIXTURE-IN-AQUEOUS SOLUTION EMULSION IN WHICH THE AQUEOUS SOLUTION IS THE CONTINUOUS PHASE, TO PRODUCE A DISPERSION IN WHICH THE AQUEOUS SOLUTION IS THE DISPERSED PHASE AND THE WAX-OIL MIXTURE IS THE CONTINUOUS PHASE; INTRODUCING A LIQUIFIED, LOW-BOILING MATERIAL INTO SAID DISPERSION; PERMITTING SAID LIQUIFIED, LOW-BOILING MATERIAL TO VAPORIZE TO PRECIPITATE WAX AND TO PRODUCE GAS; CONTINUING SAID TREATING TO ASSOCIATE SAID WAX AND SAID GAS WITH THE DISPERSED AQUEOUS SOLUTION PHASE, THEREBY PRODUCING A WAX-BEARING FROTH; AND SEPARATING SAID WAX-BEARING FROTH FROM SAID DISPERSION.
References Cited (Backward Citations)
US2062374A
Cited
US2116144A
Cited
US2153895A
Cited
US2164013A
Cited
US2263535A
Cited
US2164773A
Cited
US2161581A
Cited
US2168306A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1956-07-13 | 1957-01-12 | 1957-07-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1960-07-13 | 1961-01-12 | 1961-07-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1964-07-13 | 1965-01-12 | 1965-07-14 | $7700.00 | Window Closed / Lapsed |