GB685904A - Improvements in the separation of mixtures of isobutyl and methyl alcohols - Google Patents
Improvements in the separation of mixtures of isobutyl and methyl alcoholsInfo
- Publication number
- GB685904A GB685904A GB17384/51A GB1738451A GB685904A GB 685904 A GB685904 A GB 685904A GB 17384/51 A GB17384/51 A GB 17384/51A GB 1738451 A GB1738451 A GB 1738451A GB 685904 A GB685904 A GB 685904A
- Authority
- GB
- United Kingdom
- Prior art keywords
- column
- pipe
- gases
- methyl
- alcohol
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/74—Separation; Purification; Use of additives, e.g. for stabilisation
- C07C29/76—Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment
- C07C29/80—Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment by distillation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/74—Separation; Purification; Use of additives, e.g. for stabilisation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
- C07C31/02—Monohydroxylic acyclic alcohols
- C07C31/04—Methanol
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
<PICT:0685904/IV (b)/1> The separation of a mixture of isobutyl and methyl alcohols, in particular a mixture obtained from the reaction products of CO and H2 by treatment in a distillation column under pressure, as described in Specification 682,826, is effected by heating to slightly below the critical temperature under pressure, in particular at about the pressure at which the mixture was formed, and leading therethrough a gas free from or poor in methyl alcohol. The process may be carried out in a still, advantageously provided with a column, which may be arranged beneath the column serving for the crude separation of the synthesis products, and need have only 1/10 th the cross-section thereof. The gas free from or poor in methyl alcohol may be the initial synthesis gas or a fraction of the circulating gas freed from alcohol by cooling. Synthesis reaction product gases are led by pipe 3 into pressure column 1 at about 250 atm. and 220 DEG C. Gases escaping at 4 are cooled, and separated in 11, condensate being supplied by pump 6 to the top of the column and, by pipe 13, to the reactor, while gases are returned to the reactor by pipe 14. Part of these gases is fed by pipe 8 to still 9, heated to just above 200 DEG C. and having a column 2 in which isobutyl alcohol is freed from methyl and is withdrawn by pipe 10.ALSO:<PICT:0685904/III/1> The separation of a mixture of isobutyl and methyl alcohols, in particular a mixture obtained from the reaction products of CO and H2 by treatment in a distillation column under pressure as described in Specification 682,826 is effected by heating to slightly below the critical temperature under pressure, in particular at about the pressure at which the mixture was formed, and leading therethrough a gas free from or poor in methyl alcohol. The process may be carried out in a still, advantageously provided with a column, which may be arranged beneath the column serving for the crude separation of the synthesis products, and need have only 1/10th the cross-section thereof. The gas free from or poor in methyl alcohol may be the initial synthesis gas or a fraction of the circulating gas freed from alcohol by cooling. Synthesis reaction product gases are led by pipe 3 into pressure column 1 at about 250 atmosphere and 220 DEG C. Gases escaping at 4 are cooled, and separated in 11, condensate being supplied by pump 6 to the top of the column and, by pipe 13, to the reactor, while gases are returned to the reactor by pipe 14. Part of these gases is fed by pipe 8 to still 9, heated to just above 200 DEG C and having a column 2 in which isobutyl alcohol is freed from methyl and is withdrawn by pipe 10.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEB8391A DE844738C (en) | 1950-07-28 | 1950-07-28 | Process for the decomposition of mixtures of isobutyl and methyl alcohol |
Publications (1)
Publication Number | Publication Date |
---|---|
GB685904A true GB685904A (en) | 1953-01-14 |
Family
ID=6955812
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB17384/51A Expired GB685904A (en) | 1950-07-28 | 1951-07-23 | Improvements in the separation of mixtures of isobutyl and methyl alcohols |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE844738C (en) |
GB (1) | GB685904A (en) |
-
1950
- 1950-07-28 DE DEB8391A patent/DE844738C/en not_active Expired
-
1951
- 1951-07-23 GB GB17384/51A patent/GB685904A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
DE844738C (en) | 1952-07-24 |
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