GB647903A - Separation of close-boiling alcohols from aqueous liquid mixtures by distillation - Google Patents
Separation of close-boiling alcohols from aqueous liquid mixtures by distillationInfo
- Publication number
- GB647903A GB647903A GB21536/47A GB2153647A GB647903A GB 647903 A GB647903 A GB 647903A GB 21536/47 A GB21536/47 A GB 21536/47A GB 2153647 A GB2153647 A GB 2153647A GB 647903 A GB647903 A GB 647903A
- Authority
- GB
- United Kingdom
- Prior art keywords
- column
- water
- alcohol
- withdrawn
- per cent
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/34—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
- B01D3/36—Azeotropic 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
<PICT:0647903/III/1> Water-soluble alcohols of different molecular weights, which have close-boiling aqueous azeotropes, are separated from each other by passing the mixture, which may also contain other oxygenated organic compounds such as ketones, into the side of a fractionating column, and introducing water into the top of the column to make the water content of the internal reflux at least 65 mol. per cent and sufficient to alter the relative volatilities of the components of the feed-mixture so that a dilute aqueous solution of the alcohol of lowest molecular weight, free from the other organic components of the feed mixture, is withdrawn from the base of the column while vapours of the other components are withdrawn overhead. In an example, a mixture containing ethyl alcohol, isopropyl alcohol, methyl ethyl ketone and water was fed at 52 volumes per hour between the sections (each of 30- plates) of a fractionating column; and 2100 volumes per hour of water at 90 DEG C. was introduced into the top of the column. The reflux ratio was somewhat higher than 30 : 1. After equilibrium was reached, no detectible concentration of isopropyl alcohol or of methyl ethyl ketone was found in the aqueous ethyl alcohol bottoms. Other examples describe the separation of ethyl alcohol from the products of a Fischer synthesis. When more than one component is required to be separated in a pure state, apparatus such as that shown is employed. An aqueous mixture of narrow boiling-range containing ethyl alcohol, isopropyl alcohol, tertiary butyl alcohol and methyl ethyl ketone is fed through inlet 44 into column 41; and water is introduced into the column through inlet 45. Dilute aqueous ethyl alcohol is withdrawn through line 50 and passed to column 51 where it is concentrated; a distillate containing about 96 per cent ethyl alcohol, 4 per cent water and less than 0.1 per cent of other organic compounds, being obtained through line 57. The distillate from column 41 is passed through line 58 into column 42 where a water concentration of 90-99 mol. per cent is maintained in the internal reflux by adding water through line 62. Dilute aqueous isopropyl alcohol, free from butyl alcohol and M.E.K., is withdrawn through line 64 and concentrated in column 65. Similarly, columns 43 and 78 are used for the separation and concentration of tertiary butyl alcohol. The water withdrawn from the bottoms of columns 51, 65 and 78 is pumped back to columns 41, 42 and 43, respectively. The separation of alcohols from an olefin hydration reaction, and from a hydrocarbon oxidation reaction is referred to. Specification 598,346 is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US647903XA | 1947-01-28 | 1947-01-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB647903A true GB647903A (en) | 1950-12-28 |
Family
ID=22058292
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB21536/47A Expired GB647903A (en) | 1947-01-28 | 1947-08-07 | Separation of close-boiling alcohols from aqueous liquid mixtures by distillation |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB647903A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009090104A1 (en) * | 2008-01-18 | 2009-07-23 | Eni S.P.A. | Process for the purification of an aqueous stream coming from the fischer-tropsch reaction |
CN109824480A (en) * | 2019-02-27 | 2019-05-31 | 北控城市(北京)环境科技有限公司 | The process of ethyl alcohol in a kind of separating-purifying coal oil rectification residue |
CN115006862A (en) * | 2022-06-15 | 2022-09-06 | 浙江卫星能源有限公司 | Energy-saving high-purity n-butanol extraction system and method |
-
1947
- 1947-08-07 GB GB21536/47A patent/GB647903A/en not_active Expired
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009090104A1 (en) * | 2008-01-18 | 2009-07-23 | Eni S.P.A. | Process for the purification of an aqueous stream coming from the fischer-tropsch reaction |
US7989510B2 (en) | 2008-01-18 | 2011-08-02 | Eni S.P.A. | Process for the purification of an aqueous stream coming from the fischer-tropsch reaction |
CN109824480A (en) * | 2019-02-27 | 2019-05-31 | 北控城市(北京)环境科技有限公司 | The process of ethyl alcohol in a kind of separating-purifying coal oil rectification residue |
CN109824480B (en) * | 2019-02-27 | 2023-01-20 | 北京精刻环保科技有限公司 | Process method for separating and purifying ethanol in coal-to-liquids rectification residues |
CN115006862A (en) * | 2022-06-15 | 2022-09-06 | 浙江卫星能源有限公司 | Energy-saving high-purity n-butanol extraction system and method |
CN115006862B (en) * | 2022-06-15 | 2023-10-17 | 浙江卫星能源有限公司 | Energy-saving high-purity n-butanol extraction system and method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2649407A (en) | Separation of ethyl acetate and ethanol by azeotropic distillation with methanol | |
AU704998B2 (en) | Separation of middle boilers from a mixture of low, middle and high boilers | |
US2483246A (en) | Separation of primary, secondary, and tertiary alcohols by azeotropic distillation | |
US2575243A (en) | Extractive distillation of alcohols | |
US2371908A (en) | Recovery of olefinic hydrocarbons | |
US3819493A (en) | Process for separating halogenated hydrocarbons by extractive distillation | |
US2500329A (en) | Azeotropic distillation of 1-butanol from methyl nu-butyl ketone | |
GB1112397A (en) | Processing mixtures containing acetic acid | |
GB647903A (en) | Separation of close-boiling alcohols from aqueous liquid mixtures by distillation | |
US4012289A (en) | N-Butane/acetone separation using sulfolane | |
US2695867A (en) | Combination extraction and distillation process | |
GB647927A (en) | Extractive distillation with salt solutions | |
US2386058A (en) | Purification of organic liquids | |
US2528761A (en) | Azeotropic distillation of ethyl alcohol from methyl ethyl ketone | |
US2678905A (en) | Purification of aqueous formaldehyde solutions by extractive distillation | |
GB1063133A (en) | Separating acetic acid from reaction mixtures by distillation | |
US5380405A (en) | Separation of alpha-phellandrene from 3-carene by azeotropic distillation | |
US2671052A (en) | Methyl acetate distillation | |
US2477087A (en) | Separation and purification of methyl ethyl ketone | |
GB1092629A (en) | Separation of acetone from organic mixtures | |
US2467198A (en) | Azeotropic distillation of styrene from phenylacetylene | |
US2609333A (en) | Azeo-extractive distillation | |
US2476391A (en) | Extractive distillation of propionaldehyde from acrolein | |
JP2019516742A (en) | Process for recovering by-products from MMA | |
US3657374A (en) | Recovery of isobutylene from mixtures containing the same and butadiene |