GB647903A - Separation of close-boiling alcohols from aqueous liquid mixtures by distillation - Google Patents

Separation of close-boiling alcohols from aqueous liquid mixtures by distillation

Info

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withdrawn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
Application number
GB21536/47A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Standard Oil Development Co
Original Assignee
Standard Oil Development Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Standard Oil Development Co filed Critical Standard Oil Development Co
Publication of GB647903A publication Critical patent/GB647903A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/34Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
    • B01D3/36Azeotropic distillation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/74Separation; 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.
GB21536/47A 1947-01-28 1947-08-07 Separation of close-boiling alcohols from aqueous liquid mixtures by distillation Expired GB647903A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (6)

* Cited by examiner, † Cited by third party
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

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