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US4148834A Expired / Lapsed US ⏱️ 0.0 years remaining

Preparation of synthetic hydrocarbon lubricants

Assignee: ConocoPhillips Co
•
Filing: 1978-03-08
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Granted: 1979-04-10
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Expires: 1998-03-08
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Abstract

Abstract This disclosure concerns an improved process for preparing a synthetic hydrocarbon lubricant composition, said composition consisting essentially of di-long-chain alkyl-substituted aromatic hydrocarbons. The improved process is directed to a two-step alkylation process, using linear mono-olefins as the alkylating agent, and in which the first alkylation is conducted using HF as the catalyst, wherein the improvement comprises using aluminum chloride or aluminum bromide as the catalyst for the second alkylation step. Use of aluminum chloride or aluminum bromide, instead of HF, in the second alkylation step results in a product having better low temperature properties.

Inventors

  • 👤 Carl D. Kennedy
  • 👤 Gene E. Nicks

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 09:01
CPC Classifications
C; C10; C10M; C10M105/00; C10M105/02; C10M105/06; C07; C07C; C07C15/00; C07C15/02; C07C15/107; C07C15/113; C07C2/00; C07C2/54; C07C2/64; C07C2/66; C07C2/68; C07C2/70; C07C2527/00; C07C2527/06; C07C2527/08; C07C2527/12; C07C2527/1206; C07C2527/125; C07C2527/126; C10M2203/00; C10M2203/06

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 193 words
A process for preparing a synthetic hydrocarbon lubricant composition, consisting essentially of di-long-chain alkyl aromatic hydrocarbons, wherein the long chain alkyl groups contain about 6 to about 18 carbon atoms and wherein the aryl moiety is phenyl, tolyl, xylyl, or ethylphenyl, said process comprising: (a) contacting from 1 to 15 moles of an aromatic hydrocarbon, which is benzene, toluene, xylene, or ethylbenzene, with 1 mole of a linear monoolefin containing about 6 to about 18 carbon atoms, in the presence of about 1 to about 30 moles hydrogen fluoride at a temperature in the range of about 5° C. to about 100° C., (b) recovering from the reaction mass of step (a) mono-long-chain alkyl aromatic hydrocarbon, wherein the mono-long-chain is as defined, (c) contacting from 1 to 10 moles of the mono-long-chain alkyl aromatic hydrocarbon of step (b) with 1 mole of linear monoolefin containing about 6 to about 18 carbon atoms in the presence of from 2 to about 10 weight percent aluminum chloride or aluminum bromide, at a temperature of about 60° to about 90° C., and (d) recovering from the reaction mass of step (c) the di-long-chain alkyl aromatic hydrocarbon.
Claim 2
Dependent Claim 193 words
A process for preparing a synthetic hydrocarbon lubricant composition, consisting essentially of di-long-chain alkyl aromatic hydrocarbons, wherein the long chain alkyl groups contain about 6 to about 18 carbon atoms and wherein the aryl moiety is phenyl, tolyl, xylyl, or ethylphenyl, said process comprising: (a) contacting from 1 to 15 moles of an aromatic hydrocarbon, which is benzene, toluene, xylene, or ethylbenzene, with 1 mole of a linear monoolefin containing about 6 to about 18 carbon atoms, in the presence of about 1 to about 30 moles hydrogen fluoride at a temperature in the range of about 5° C. to about 100° C., (b) recovering from the reaction mass of step (a) mono-long-chain alkyl aromatic hydrocarbon, wherein the mono-long-chain is as defined, (c) contacting from 1 to 10 moles of the mono-long-chain alkyl aromatic hydrocarbon of step (b) with 1 mole of linear monoolefin containing about 6 to about 18 carbon atoms in the presence of from 2 to about 10 weight percent aluminum chloride or aluminum bromide, at a temperature of about 60° to about 90° C., and (d) recovering from the reaction mass of step (c) the di-long-chain alkyl aromatic hydrocarbon.
Claim 3
Dependent Claim 40 words
The process of claim 1 wherein step (a) is conducted using the following conditions: (a) moles of aromatic hydrocarbon to moles of olefin 2 to 10, and (b) moles of hydrogen fluoride to moles of aromatic hydrocarbon: 1 to 10.
Claim 4
Dependent Claim 25 words
The process of claim 2 wherein the amount of catalyst in step (c) is about 3 to about 6 weight percent, based on the olefin.
Claim 5
Dependent Claim 11 words
The process of claim 3 wherein the aromatic hydrocarbon is benzene.
Claim 6
Dependent Claim 18 words
The process of claim 4 wherein the product has a maximum viscosity at -40° F. of 12,000 centistokes.
Claim 7
Dependent Claim 18 words
The process of claim 5 wherein the product has a maximum viscosity at -40° F. of 10,000 centistokes.
Claim 8
Dependent Claim 191 words
A process for preparing a synthetic hydrocarbon lubricant composition, consisting essentially of di-alkyl-benzenes, wherein the alkyl groups are linear and contain about 10 to about 14 carbon atoms, said process comprising: (a) contacting from 1 to 15 moles of benzene with 1 mole of a linear monoolefin containing about 10 to about 14 carbon atoms in the presence of about 1 to about 30 moles of hydrogen fluoride, at a temperature in the range of about 5° C. to about 100° C., (b) recovering from the reaction mass of step (a) monoalkylbenzene wherein the alkyl group is linear and contains from about 10 to about 14 carbon atoms, (c) contacting from 1 to 10 moles of the monoalkylbenzene of step (b) with 1 mole of linear monoolefin containing from about 10 to about 14 carbon atoms in the presence of from 2 to 10 weight percent aluminum chloride or aluminum bromide, at a temperature of about 60 to about 90° C., and (d) recovering from the reaction mass of step (c) the di-C 10 -C 14 alkylbenzene, said product having a viscosity at -40° F. of not more than 12,000 centistokes.
Claim 9
Dependent Claim 191 words
A process for preparing a synthetic hydrocarbon lubricant composition, consisting essentially of di-alkyl-benzenes, wherein the alkyl groups are linear and contain about 10 to about 14 carbon atoms, said process comprising: (a) contacting from 1 to 15 moles of benzene with 1 mole of a linear monoolefin containing about 10 to about 14 carbon atoms in the presence of about 1 to about 30 moles of hydrogen fluoride, at a temperature in the range of about 5° C. to about 100° C., (b) recovering from the reaction mass of step (a) monoalkylbenzene wherein the alkyl group is linear and contains from about 10 to about 14 carbon atoms, (c) contacting from 1 to 10 moles of the monoalkylbenzene of step (b) with 1 mole of linear monoolefin containing from about 10 to about 14 carbon atoms in the presence of from 2 to 10 weight percent aluminum chloride or aluminum bromide, at a temperature of about 60 to about 90° C., and (d) recovering from the reaction mass of step (c) the di-C 10 -C 14 alkylbenzene, said product having a viscosity at -40° F. of not more than 12,000 centistokes.
Claim 10
Dependent Claim 38 words
The process of claim 7 wherein step (a) is conducted using the following conditions: (a) moles of benzene to moles of olefin: 2 to 10, and (b) moles of hydrogen fluoride to moles of benzene: 1 to 10.
Claim 11
Dependent Claim 25 words
The process of claim 8 wherein the amount of catalyst in step (c) is about 3 to about 6 weight percent, based on the olefin.
Claim 12
Dependent Claim 18 words
The process of claim 9 wherein the product has a maximum viscosity at -40° F. of 10,000 centistokes.

References Cited (Backward Citations)

US2479120A Cited
US2467130A Cited
US2525778A Cited
US2626967A Cited
US2871254A Cited
US3173965A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-04-09 1982-10-09 1983-04-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-04-09 1986-10-09 1987-04-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-04-09 1990-10-09 1991-04-10 $7700.00 Window Closed / Lapsed

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