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US4256465A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for producing methyl tert-butyl ether and fuel composition containing the same

Assignee: Eneos Corp
•
Filing: 1979-07-20
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Granted: 1981-03-17
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Expires: 1999-07-20
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Abstract

Abstract A method for producing methyl tert-butyl ether which comprises the steps of: allowing isobutylene-containing hydrocarbon and methyl alcohol in a given molar ratio to react at a given temperature, pressure and liquid space velocity in the presence of strongly acidic cation-exchange resin catalyst; then passing the reaction product through a fixed bed filled with a water-insoluble, solid particulate acid-neutralizing agent; and subjecting the effluent to flashing operation, preferably also to rectification, to obtain methyl tert-butyl ether. Further included in the invention is the preparation of a fuel composition by mixing the thus obtained methyl tert-butyl ether into an internal combustion fuel.

Inventors

  • 👤 Tetsuya Takezono
  • 👤 Yasuo Fujiwara

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 19:13
CPC Classifications
C; C10; C10L; C10L10/00; C10L10/10; C07; C07C; C07C41/00; C07C41/01; C07C41/05; C07C41/06; C10L1/00; C10L1/02; C10L1/10; C10L1/14; C10L1/18; C10L1/185; C10L1/1852; C10L10/02

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 229 words
A method for preparing a fuel composition for internal combustion engines comprising the steps of: (A) allowing isobutylene and methyl alcohol to react with each other by continuously passing an isobutylene-containing hydrocarbon mixture and methyl alcohol through a fixed bed filled with strongly acidic cation-exchange resin particles of 0.2 to 10 mm in mean grain diameter, at a temperature of 0° to 100° C., a pressure of 1 to 50 atmospheres and a liquid space velocity of 0.1 to 50 (1/hr), the molar ratio of isobutylene in said mixture to said methyl alcohol being in the range of 1:0.6 to 1:1.4; (B) dividing the effluent from the reaction of step (A) into first and second parts in which the weight ratio of said first part to said second part is in the range from 1:3 to 1:15; (C) recycling said second part to the fixed bed in step (A); (D) passing said first part through a fixed bed filled with a water-insoluble, solid, particulate acid-neutralizing agent of 0.1 to 10 mm in mean grain diameter, at 0° to 100° C.; (E) introducing the neutralized first part into a flashing tower to flash-remove unreacted hydrocarbon and to recover a methyl tert-butyl ether containing mixture from the bottom of said flashing tower; and, (F) mixing 2 to 30% by volume of said methyl tert-butyl ether containing mixture with internal combustion fuel.
Claim 2
Independent Claim 229 words
A method for preparing a fuel composition for internal combustion engines comprising the steps of: (A) allowing isobutylene and methyl alcohol to react with each other by continuously passing an isobutylene-containing hydrocarbon mixture and methyl alcohol through a fixed bed filled with strongly acidic cation-exchange resin particles of 0.2 to 10 mm in mean grain diameter, at a temperature of 0° to 100° C., a pressure of 1 to 50 atmospheres and a liquid space velocity of 0.1 to 50 (1/hr), the molar ratio of isobutylene in said mixture to said methyl alcohol being in the range of 1:0.6 to 1:1.4; (B) dividing the effluent from the reaction of step (A) into first and second parts in which the weight ratio of said first part to said second part is in the range from 1:3 to 1:15; (C) recycling said second part to the fixed bed in step (A); (D) passing said first part through a fixed bed filled with a water-insoluble, solid, particulate acid-neutralizing agent of 0.1 to 10 mm in mean grain diameter, at 0° to 100° C.; (E) introducing the neutralized first part into a flashing tower to flash-remove unreacted hydrocarbon and to recover a methyl tert-butyl ether containing mixture from the bottom of said flashing tower; and, (F) mixing 2 to 30% by volume of said methyl tert-butyl ether containing mixture with internal combustion fuel.
Claim 3
Independent Claim 282 words
A method for preparing a fuel composition for internal combustion engines comprising the steps of: (A) allowing isobutylene and methyl alcohol to react with each other by continuously passing an isobutylene-containing hydrocarbon mixture and methyl alcohol through a fixed bed filled with strongly acidic cation-exchange resin particles of 0.2 to 10 mm in mean grain diameter, at a temperature of 0° to 100° C., a pressure of 1 to 50 atmospheres and a liquid space velocity of 0.1 to 50 (1/hr), the molar ratio of isobutylene in said mixture to said methyl alcohol being in the range of 1:0.6 to 1:1.4; (B) dividing the effluent from the reaction step (A) into first and second parts in which the weight ratio of said first part to said second part is in the range from 1:3 to 1:15; (C) recycling said second part to the fixed bed in step (A); (D) passing said first part through a fixed bed filled with a water-insoluble, solid, particulate acid-neutralizing agent of 0.1 to 10 mm in mean grain diameter, at 0° to 10° C.; (E) introducing the neutralized first part into a flashing tower to flash-remove unreacted hydrocarbon and to recover a methyl tert-butyl ether containing mixture from the bottom of said flashing tower; (F) distilling said methyl tert-butyl ether-containing mixture with a multistage distillation column to remove an azeotropic mixture of methyl tert-butyl ether and methyl alcohol from the top of said distillation column and to recycle said azeotropic mixture for reuse in step (A), thereby obtaining methyl tert-butyl ether from the bottom of said distillation column; and (G) mixing 2 to 30% by volume of said methyl tert-butyl ether containing mixture with internal combustion fuel.
Claim 4
Independent Claim 282 words
A method for preparing a fuel composition for internal combustion engines comprising the steps of: (A) allowing isobutylene and methyl alcohol to react with each other by continuously passing an isobutylene-containing hydrocarbon mixture and methyl alcohol through a fixed bed filled with strongly acidic cation-exchange resin particles of 0.2 to 10 mm in mean grain diameter, at a temperature of 0° to 100° C., a pressure of 1 to 50 atmospheres and a liquid space velocity of 0.1 to 50 (1/hr), the molar ratio of isobutylene in said mixture to said methyl alcohol being in the range of 1:0.6 to 1:1.4; (B) dividing the effluent from the reaction step (A) into first and second parts in which the weight ratio of said first part to said second part is in the range from 1:3 to 1:15; (C) recycling said second part to the fixed bed in step (A); (D) passing said first part through a fixed bed filled with a water-insoluble, solid, particulate acid-neutralizing agent of 0.1 to 10 mm in mean grain diameter, at 0° to 10° C.; (E) introducing the neutralized first part into a flashing tower to flash-remove unreacted hydrocarbon and to recover a methyl tert-butyl ether containing mixture from the bottom of said flashing tower; (F) distilling said methyl tert-butyl ether-containing mixture with a multistage distillation column to remove an azeotropic mixture of methyl tert-butyl ether and methyl alcohol from the top of said distillation column and to recycle said azeotropic mixture for reuse in step (A), thereby obtaining methyl tert-butyl ether from the bottom of said distillation column; and (G) mixing 2 to 30% by volume of said methyl tert-butyl ether containing mixture with internal combustion fuel.
Claim 5
Independent Claim 51 words
The method for preparing a fuel composition as defined in claims 1 or 2, wherein said internal combustion fuel is at least one member selected from the group consisting of alcohols having 1 to 4 carbon atoms, ethers having 4 to 8 carbon atoms and hydrocarbons boiling in the gasoline range.
Claim 6
Dependent Claim 50 words
The methods of claims 1 or 2, wherein said molar ratio of isobutylene to said methyl alcohol is in the range of 1:1 to 1:1.3, a liquid space velocity of 0.5-15 (1/hr) is employed in step (A) and a liquid space velocity of 0.1-20 (1/hr) is employed in step (D).
Claim 7
Dependent Claim 11 words
The method of claim 4, wherein said neutralizing agent is hydrotalcite.
Claim 8
Dependent Claim 23 words
The method of claim 5, wherein said hydrotalcite is a natural hydrotalcite having a molar ratio of magnesium to aluminum of about 3.
Claim 9
Dependent Claim 22 words
The method of claim 4, wherein said hydrotalcite is a synthetic hydrotalcite having a molar ratio of magnesium to aluminum of 1-10.

References Cited (Backward Citations)

US2839569A Cited
US2855437A Cited
US2958626A Cited
GB957000A Cited
US3539306A Cited
US3920582A Cited
US4039590A Cited
US3940450A Cited
DE2707765A1 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-03-16 1984-09-15 1985-03-17 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-03-16 1988-09-15 1989-03-17 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-03-16 1992-09-15 1993-03-17 $7700.00 Window Closed / Lapsed

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