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
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.
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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 |