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US4013521A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for purifying methanol by distillation

Assignee: Imperial Chemical Industries Ltd
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Filing: 1975-01-29
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Granted: 1977-03-22
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Expires: 1995-01-29
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Abstract

Abstract Impure methanol containing ethanol is substantially freed of ethanol by distilling a mixture consisting essentially of the impure methanol, ethanol and water with the aid of a distillation column in a region of which the methanol to water ratio is maintained substantially constant, and withdrawing a stream enriched in ethanol from a point near one end of that region.

Inventors

  • 👤 Roger Hardiman Scott

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 13:34
CPC Classifications
C; C07; C07C; C07C29/00; C07C29/74; C07C29/76; C07C29/80; Y; Y10; Y10S; Y10S203/00; Y10S203/20; Y10S203/24

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 124 words
A process for purifying methanol from a starting mixture of synthetic crude methanol consisting essentially of methanol, 8 to 30% by weight water and up to 0.5% by weight ethanol comprising: a. feeding said starting mixture to a distillation column at a level which when said column is in equilibrium operation, the water content within said column at said level is lower than in said mixture producing over a region of the column below the feed level a substantially constant methanol to water weight ratio, b. withdrawing water as bottoms, c. withdrawing product methanol from the upper part of the column, and d. withdrawing a side stream enriched in ethanol from a level below the end of the region remote from the feed level.
Claim 2
Dependent Claim 124 words
A process for purifying methanol from a starting mixture of synthetic crude methanol consisting essentially of methanol, 8 to 30% by weight water and up to 0.5% by weight ethanol comprising: a. feeding said starting mixture to a distillation column at a level which when said column is in equilibrium operation, the water content within said column at said level is lower than in said mixture producing over a region of the column below the feed level a substantially constant methanol to water weight ratio, b. withdrawing water as bottoms, c. withdrawing product methanol from the upper part of the column, and d. withdrawing a side stream enriched in ethanol from a level below the end of the region remote from the feed level.
Claim 3
Dependent Claim 25 words
A process according to claim 1 in which the ethanol enriched stream is withdrawn at the point at which the methanol mole fraction is 0.4.
Claim 4
Dependent Claim 19 words
A process according to claim 1 wherein said region occupies 10 to 20% of the length of the column.
Claim 5
Dependent Claim 169 words
A process for purifying methanol from a starting mixture of synthetic crude methanol comprising: a. subjecting a crude methanol mixture to water extractive distillation and removing a methanol-containing stream as bottoms: b. subjecting said methanol containing stream as bottoms to a coarse distillation separation of methanol wherein the methanol containing stream is collected overhead to produce a starting mixture consisting essentially of methanol, 8 to 30% by weight water and up to 0.5% by weight ethanol; c. feeding said starting mixture to a distillation column at a level which when said column is in equilibrium operation, the water content is lower within said column at said level than in said mixture producing over a region of the column below the feed level a substantially constant methanol to water weight ratio; d. withdrawing water as bottoms, e. withdrawing product methanol from the upper part of the column, and f. withdrawing a side stream enriched in ethanol from a level below the end of the region remote from the feed level.
Claim 6
Dependent Claim 169 words
A process for purifying methanol from a starting mixture of synthetic crude methanol comprising: a. subjecting a crude methanol mixture to water extractive distillation and removing a methanol-containing stream as bottoms: b. subjecting said methanol containing stream as bottoms to a coarse distillation separation of methanol wherein the methanol containing stream is collected overhead to produce a starting mixture consisting essentially of methanol, 8 to 30% by weight water and up to 0.5% by weight ethanol; c. feeding said starting mixture to a distillation column at a level which when said column is in equilibrium operation, the water content is lower within said column at said level than in said mixture producing over a region of the column below the feed level a substantially constant methanol to water weight ratio; d. withdrawing water as bottoms, e. withdrawing product methanol from the upper part of the column, and f. withdrawing a side stream enriched in ethanol from a level below the end of the region remote from the feed level.
Claim 7
Dependent Claim 152 words
A process for producing purified methanol comprising: a. subjecting a crude methanol mixture containing as impurities water, ethanol and low boiling impurities to a distillation in which said mixture is freed of components boiling at a the boiling point of methanol to produce a starting mixture of methanol, 8 to 30% by weight water and up to 0.5% ethanol; b. feeding said starting mixture to a distillation column at a level which when said column is in equilibrium operation, the water content is lower within said column at said level than in said mixture producing over a region of the column below the feed level a substantially constant methanol to water weight ratio; c. withdrawing water as bottoms, d. withdrawing product methanol from the upper part of the column, and e. withdrawing a side stream enriched in ethanol from a level below the end of the region remote from the feed level.
Claim 8
Dependent Claim 152 words
A process for producing purified methanol comprising: a. subjecting a crude methanol mixture containing as impurities water, ethanol and low boiling impurities to a distillation in which said mixture is freed of components boiling at a the boiling point of methanol to produce a starting mixture of methanol, 8 to 30% by weight water and up to 0.5% ethanol; b. feeding said starting mixture to a distillation column at a level which when said column is in equilibrium operation, the water content is lower within said column at said level than in said mixture producing over a region of the column below the feed level a substantially constant methanol to water weight ratio; c. withdrawing water as bottoms, d. withdrawing product methanol from the upper part of the column, and e. withdrawing a side stream enriched in ethanol from a level below the end of the region remote from the feed level.

References Cited (Backward Citations)

US3239435A Cited
US3282802A Cited
US3293154A Cited
US3434937A Cited
US3406100A Cited
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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) 1980-03-21 1980-09-20 1981-03-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-03-21 1984-09-20 1985-03-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-03-21 1988-09-20 1989-03-22 $7700.00 Window Closed / Lapsed

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