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US4068056A Expired / Lapsed US ⏱️ 0.0 years remaining

Aminated polymeric additives for fuel and lubricants

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1975-03-05
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Granted: 1978-01-10
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Expires: 1995-03-05
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Abstract

Abstract Aminated polymers, resulting from the reaction of a hydrocarbon polymer with an oxygen-containing gas and an amine compound at elevated temperatures of from about 130 DEG C. to about 300 DEG C. provide a multi-functional additive for lubricants and hydrocarbon fuels. This reaction can be carried out if desired in an oil solution. The resulting aminated polymers are useful as sludge dispersants for fuel lubricants. When the aminated polymers have a high molecular weight, they are also useful as viscosity-index improvers with dispersant and/or pour point depressant activity.

Inventors

  • 👤 Lawrence J. Engel
  • 👤 John B. Gardiner

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 22:42
CPC Classifications
C; C10; C10M; C10M143/00; C10M143/18; C10L; C10L1/00; C10L1/10; C10L1/14; C10L1/22; C10L1/221; C10M2207/00; C10M2207/02; C10M2207/023; C10M2207/028; C10M2207/28; C10M2207/282; C10M2207/32; C10M2207/34; C10M2209/00; C10M2209/10; C10M2209/103; C10M2209/109; C10M2209/11; C10M2209/111; C10M2209/112; C10M2215/00; C10M2215/02; C10M2215/04; C10M2215/042; C10M2215/044; C10M2215/22; C10M2215/221; C10M2215/223; C10M2215/224; C10M2215/225; C10M2215/226; C10M2215/24; C10M2215/26; C10M2215/30; C10M2217/00; C10M2217/02; C10M2217/04; C10M2217/046; C10M2217/06; C10M2219/00; C10M2219/08; C10M2219/082; C10M2223/00; C10M2223/02; C10M2223/04; C10M2223/042; C10M2223/045; C10N; C10N2010/00; C10N2010/04; C10N2040/00; C10N2040/04; C10N2040/042; C10N2040/044; C10N2040/046; C10N2040/08; C10N2070/00; C10N2070/02

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 180 words
In a process for aminating a degraded-oxygenated copolymer by reaction with a primary or secondary amine or polyamine to form an oil-soluble sludge dispersing, viscosity-index improving additive for normally liquid hydrocarbon fuels and lubricating oils, the improvement which comprises concurrently reacting a Ziegler-Natta catalyzed polymer with a hydrocarbyl polyamine having from 2 to 60 total carbon atoms and from 2 to 6 nitrogen atoms in the presence of an oxygen-containing gas and at an elevated temperature of from about 130° C. to about 300° C. for from 0.5 to about 12 hours and at a pressure ranging from 0.1 to 20 atmospheres, said polymer being a copolymer of ethylene and one or more C 3 to C 28 alpha-olefins, and characterized by: an ethylene content in the range of about 2 to 98 weight percent; a degree of crystallinity of less than about 25 wt. %; and, a weight average molecular weight of from about 2,000 to 800,000 wherein said improvement provides means for introducing from about 0.01 to 0.8 wt. % nitrogen into said polymer enhancing its dispersancy activity.
Claim 2
Dependent Claim 180 words
In a process for aminating a degraded-oxygenated copolymer by reaction with a primary or secondary amine or polyamine to form an oil-soluble sludge dispersing, viscosity-index improving additive for normally liquid hydrocarbon fuels and lubricating oils, the improvement which comprises concurrently reacting a Ziegler-Natta catalyzed polymer with a hydrocarbyl polyamine having from 2 to 60 total carbon atoms and from 2 to 6 nitrogen atoms in the presence of an oxygen-containing gas and at an elevated temperature of from about 130° C. to about 300° C. for from 0.5 to about 12 hours and at a pressure ranging from 0.1 to 20 atmospheres, said polymer being a copolymer of ethylene and one or more C 3 to C 28 alpha-olefins, and characterized by: an ethylene content in the range of about 2 to 98 weight percent; a degree of crystallinity of less than about 25 wt. %; and, a weight average molecular weight of from about 2,000 to 800,000 wherein said improvement provides means for introducing from about 0.01 to 0.8 wt. % nitrogen into said polymer enhancing its dispersancy activity.
Claim 3
Dependent Claim 53 words
A process according to claim 1, wherein said amine has the general formula: ##STR3##wherein s is 2 to 6 and t is 0 to 10 and is present in less than about 1 wt. % based upon the weight of said polymer whereby pour point depressant activity is additionally provided to said additive.
Claim 4
Dependent Claim 22 words
A process according to claim 2 wherein said amine is tetraethylene pentamine and said copolymer is a copolymer of ethylene and propylene.
Claim 5
Dependent Claim 21 words
Process according to claim 2, wherein said copolymer is a copolymer of ethylene and propylene, and said amine is triethylene tetraamine.

References Cited (Backward Citations)

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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) 1981-01-09 1981-07-11 1982-01-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-01-09 1985-07-11 1986-01-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-01-09 1989-07-11 1990-01-10 $7700.00 Window Closed / Lapsed

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