Patent US4262145A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4262145A Expired / Lapsed US ⏱️ 0.0 years remaining

Novel etherification process

Assignee: Chevron USA Inc
•
Filing: 1979-12-10
•
Granted: 1981-04-14
•
Expires: 1999-12-10
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A process for converting an olefin, or a mixture of olefins, to an ether, or a mixture of ethers, which comprises reacting said olefin, or said mixture of olefins, with an alkanol in contact with silicatungstic acid.

Inventors

  • 👤 Charles M. Selwitz
  • 👤 John G. McNulty

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 12:36
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/05; C07C41/06

Claims Analysis

Total Claims: 24
Claim 1
Independent Claim 182 words
A process for converting an olefin, or mixture of olefins, to an ether, or a mixture of ethers, said olefin being a branched olefin or a diolefin defined by the following structure: ##STR3## wherein R 1 is hydrogen, alkyl or alkenyl; but when R 1 is alkenyl R 2 and R 3 are hydrogen or alkyl; and when R 1 is hydrogen or alkyl, R 2 and R 3 are alkyls; said alkyls and alkenyls having from one to 12 carbon atoms, which comprises reacting in batch form in liquid phase said olefins, or mixtures of olefins, with an alkanol, or mixtures of alkanols, selected from the group consisting of methanol, ethanol, normal propanol and isopropanol, in a molar ratio of alkanol to olefin from about 1:1 to about 15:1, in contact with silicatungstic acid, with the weight of catalyst per weight of reaction solution being about 1:100 to about 1:1, at a temperature of about 50° to about 200° C. and a pressure of about 0.1 to about 10 atmospheres for about one minute to about 12 hours or even longer.
Claim 2
Dependent Claim 182 words
A process for converting an olefin, or mixture of olefins, to an ether, or a mixture of ethers, said olefin being a branched olefin or a diolefin defined by the following structure: ##STR3## wherein R 1 is hydrogen, alkyl or alkenyl; but when R 1 is alkenyl R 2 and R 3 are hydrogen or alkyl; and when R 1 is hydrogen or alkyl, R 2 and R 3 are alkyls; said alkyls and alkenyls having from one to 12 carbon atoms, which comprises reacting in batch form in liquid phase said olefins, or mixtures of olefins, with an alkanol, or mixtures of alkanols, selected from the group consisting of methanol, ethanol, normal propanol and isopropanol, in a molar ratio of alkanol to olefin from about 1:1 to about 15:1, in contact with silicatungstic acid, with the weight of catalyst per weight of reaction solution being about 1:100 to about 1:1, at a temperature of about 50° to about 200° C. and a pressure of about 0.1 to about 10 atmospheres for about one minute to about 12 hours or even longer.
Claim 3
Dependent Claim 15 words
The process of claim 1 wherein said olefin has from four to 14 carbon atoms.
Claim 4
Dependent Claim 15 words
The process of claim 1 wherein said olefin has from four to 10 carbon atoms.
Claim 5
Dependent Claim 18 words
The process of claim 1 wherein said alkyls and said alkenyls have from one to eight carbon atoms.
Claim 6
Dependent Claim 10 words
The process of claim 1 wherein R 1 is hydrogen.
Claim 7
Dependent Claim 11 words
The process of claim 1 wherein R 1 is an alkyl.
Claim 8
Dependent Claim 11 words
The process of claim 1 wherein R 1 is an alkenyl.
Claim 9
Dependent Claim 13 words
The process of claim 1 wherein R 2 and R 3 are hydrogen.
Claim 10
Dependent Claim 13 words
The process of claim 1 wherein R 2 and R 3 are alkyls.
Claim 11
Dependent Claim 12 words
The process of claim 1 wherein said olefin is a branched olefin.
Claim 12
Dependent Claim 11 words
The process of claim 1 wherein said olefin is a diolefin.
Claim 13
Dependent Claim 10 words
The process of claim 1 wherein said alkanol is methanol.
Claim 14
Dependent Claim 10 words
The process of claim 1 wherein said alkanol is ethanol.
Claim 15
Dependent Claim 11 words
The process of claim 1 wherein said alkanol is normal propanol.
Claim 16
Dependent Claim 10 words
The process of claim 1 wherein said alkanol is isopropanol.
Claim 17
Dependent Claim 20 words
The process of claim 1 wherein the molar ratio of alkanol to olefin is from about 2:1 to about 5:1.
Claim 18
Dependent Claim 21 words
The process of claim 1 wherein the weight of catalyst per weight of reaction solution is about 1:4 to about 1:40.
Claim 19
Dependent Claim 16 words
The process of claim 1 wherein the reaction temperature is about 80° to about 120° C.
Claim 20
Dependent Claim 11 words
The process of claim 1 wherein the pressure is about atmospheric.
Claim 21
Dependent Claim 16 words
The process of claim 1 wherein the reaction time is about one-half to about four hours.
Claim 22
Dependent Claim 17 words
The process of claim 1 wherein said silicatungstic acid has the formula: SiO 2 .12WO 3 .
Claim 23
Dependent Claim 27 words
The process of claim 1 wherein said silicatungstic acid is deposited on silica in an acid to silica weight ratio of about five to about 100 percent.
Claim 24
Dependent Claim 27 words
The process of claim 1 wherein said silicatungstic acid is deposited on silica in an acid to silica weight ratio of about 30 to about 100 percent.

References Cited (Backward Citations)

US2067385A Cited
US3135807A Cited
US4175210A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-04-13 1984-10-13 1985-04-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-04-13 1988-10-13 1989-04-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-04-13 1992-10-13 1993-04-14 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag