US4382004A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Preparation of magnesium alkylphenates and their use as detergent-dispersant additives for lubricating oils
Assignee: Orogil SA
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Filing: 1981-08-03
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Granted: 1983-05-03
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Expires: 2001-08-03
Abstract
Abstract A method of preparing magnesium alkylphenates comprising: 1. preparing a suspension of "active" magnesium oxide in methanol; 2. contacting said suspension with a mixture containing (a) an alkylphenol bearing one or more C 6 -C 60 alkyl substituents; (b) a dilution oil; (c) and optionally a heavy alcohol of a boiling point of between 100° and 200° C., the ratio of number of mols of "active" magnesium oxide to number of recurrent phenolic OH units being between about 0.25 and 2; and 3. carbonating the resultant medium under pressure with carbon dioxide. The magnesium alkylphenates thus obtained are suitable detergent-dispersant additives for lubricating oils in amounts of between about 1 and 8 percent of the weight of the oils.
Inventors
- 👤 Jean-Pierre Tassara
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 10:46
CPC Classifications
C; C10; C10M; C10M159/00; C10M159/12; C10M159/20; C10M159/22
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
212 words
A method of preparing magnesium alkyl phenates comprising: (A) preparing a suspension of active magnesium oxide in methanol, said suspension containing up to about 10 percent by weight of active magnesium oxide, referred to the weight of the methanol; (B) contacting at a temperature between about 0° and 40° C. said suspension with a mixture consisting essentially of: (a) an alkyl phenol having at least one C 6 -C 60 alkyl substituent, (b) a dilution oil, and (c) a heavy alcohol of a boiling point of between about 100° and 200° C. that is not a diol, the ratio of the number of mols of active magnesium oxide to the number of recurrent phenolic OH units being between about 0.25 and 2, the amount of dilution oil being between about 0 and 140 percent by weight, referred to the weight of alkyl phenol, and the molar ratio of heavy alcohol to active magnesium oxide being between about 0 and 4, the said molar ratio being at least 1.2 when the ratio of the number of active magnesium oxide mols to the number of recurrent phenolic OH units is greater than about 0.75; (C) and carbonating the resultant medium under pressure with carbon dioxide at a temperature between about 0° and 40° C.
Claim 2
Independent Claim
212 words
A method of preparing magnesium alkyl phenates comprising: (A) preparing a suspension of active magnesium oxide in methanol, said suspension containing up to about 10 percent by weight of active magnesium oxide, referred to the weight of the methanol; (B) contacting at a temperature between about 0° and 40° C. said suspension with a mixture consisting essentially of: (a) an alkyl phenol having at least one C 6 -C 60 alkyl substituent, (b) a dilution oil, and (c) a heavy alcohol of a boiling point of between about 100° and 200° C. that is not a diol, the ratio of the number of mols of active magnesium oxide to the number of recurrent phenolic OH units being between about 0.25 and 2, the amount of dilution oil being between about 0 and 140 percent by weight, referred to the weight of alkyl phenol, and the molar ratio of heavy alcohol to active magnesium oxide being between about 0 and 4, the said molar ratio being at least 1.2 when the ratio of the number of active magnesium oxide mols to the number of recurrent phenolic OH units is greater than about 0.75; (C) and carbonating the resultant medium under pressure with carbon dioxide at a temperature between about 0° and 40° C.
Claim 3
Dependent Claim
142 words
A method according to claim 1, wherein there are employed: (A) from about 5 to 10 percent by weight of active magnesium oxide, referred to the weight of methanol; (B) a ratio of number of mols of active magnesium oxide to number of recurrent phenolic OH units of between about 0.5 and 1; (C) from about 20 to 75 percent by weight of dilution oil, referred to the weight of alkylphenol; ;p1 (D) a molar ratio of heavy alcohol to active magnesium oxide of at least 1.5 when the ratio of the number of mols of active magnesium oxide to number of recurrent phenolic OH units is greater than about 0.75; and (E) the carbonation operation is carried out with an amount of CO 2 corresponding, within about 30 percent by weight, to that which can be completely absorbed by the medium.
Claim 4
Dependent Claim
35 words
A method according to claim 1 or claim 2, wherein the carbonation operation is carried out for at least about 4 hours at a pressure of between about 3 and 30 kg. per square centimeter.
Claim 5
Dependent Claim
54 words
A method according to claim 1 or 2, wherein the carbonation operation is carried out at a pressure of between about 5 and 15 kg. per square centimeter, at a temperature of between about 15° and 30° C., and with an amount of CO 2 corresponding substantially to that which can be completely absorbed.
Claim 6
Dependent Claim
42 words
A method according to claim 1, wherein the suspension of active magnesium oxide in methanol is precarbonated under pressure before contacting it with the mixture of alkyl phenol with oil and heavy alcohol, by contacting under pressure, and by terminating the carbonation.
Claim 7
Dependent Claim
29 words
A method according to claim 5, wherein the pressure is between about 3 and 30 kg. per square centimeter and the temperature is between about zero and 40° C.
Claim 8
Dependent Claim
55 words
A method according to claim 6, wherein there are employed a pressure of between about 5 and 15 kg. per square centimeter and a temperature of between about 15° and 30° C., and the precarbonation operation lasts at least about three hours, and the precarbonation and carbonation operations together last at least about 4 hours.
Claim 9
Dependent Claim
23 words
A method according to claim 1, wherein the alkyl phenol bears at least one C 9 -C 15 alkyl substituent and is sulfurized.
Claim 10
Dependent Claim
25 words
A method according to claim 1, wherein the heavy alcohol used is a member selected from the class consisting of isobutanol, hexanol, or 2-ethyl hexanol.
Claim 11
Dependent Claim
54 words
A method according to claim 1, wherein the carbonation operation is followed by a treatment with about 1 to 2 mols of water per mol of active magnesium oxide when the ratio of the number of mols of active magnesium oxide to the number of recurrent phenolic OH units is greater than about 1.
Claim 12
Dependent Claim
12 words
A lubricating oil additive as obtained by the method of claim 1.
Claim 13
Dependent Claim
14 words
A detergent-dispersant additive for lubricating oils, obtained by the method defined by claim 1.
Claim 14
Dependent Claim
32 words
A novel lubricating composition, having desirable detergent and dispersion properties, comprising an oil containing between about 1 and 8 percent by weight of a novel lubricant additive composition according to claim 12.
Claim 15
Dependent Claim
29 words
A gasoline engine oil, having desirable detergent and dispersion properties, containing between about 1 and 4 percent by weight of a novel lubricant additive composition according to claim 12.
Claim 16
Dependent Claim
30 words
A novel diesel engine oil having desirable detergent and dispersion properties containing between about 1 and 8 percent by weight of a novel lubricant additive composition according to claim 12.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1986-05-02 | 1986-11-01 | 1987-05-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-05-02 | 1990-11-01 | 1991-05-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-05-02 | 1994-11-01 | 1995-05-03 | $7700.00 | Window Closed / Lapsed |