GB788931A - Improvements in or relating to the separation of organic mixtures - Google Patents
Improvements in or relating to the separation of organic mixturesInfo
- Publication number
- GB788931A GB788931A GB2219854A GB2219854A GB788931A GB 788931 A GB788931 A GB 788931A GB 2219854 A GB2219854 A GB 2219854A GB 2219854 A GB2219854 A GB 2219854A GB 788931 A GB788931 A GB 788931A
- Authority
- GB
- United Kingdom
- Prior art keywords
- ketone
- acids
- mixture
- acid
- formaldehyde
- 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
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/78—Separation; Purification; Stabilisation; Use of additives
- C07C45/81—Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation
- C07C45/82—Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation by distillation
- C07C45/84—Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation by distillation by azeotropic distillation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
- C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
- C07C51/44—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation
- C07C51/46—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation by azeotropic distillation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The components of a mixture of one or more aliphatic carboxylic acids, water and formaldehyde are separated by rectifying the mixture in a distillation column in the presence of an auxiliary organic liquid which is insoluble in water and, which forms with water and formaldehyde, but not with the acid or acids, an azeotropic mixture having a boiling-point below that of the acid or acids, recovering anhydrous acid or acids from the base of the column and separating formaldehyde as an aqueous solution from a heterogeneous liquid phase condensed from the vapour phase of the column. The auxiliary organic liquid may be di-isopropyl ether, di-butyl ether, isopropyl or butyl formates or acetates, methyl isopropyl ketone, or methyl isobutyl ketone, when the acids are formic acid and acetic acid. A mixture also containing a ketone having a boiling-point below that of the acid or acids, such as acetone, may also be separated using an auxiliary organic liquid incapable of forming a binary azeotrope with the ketone or a ternary azeotrope with the ketone and water, and the boiling-point of the azeotropic mixture which it forms with formaldehyde and water must be between that of the ketone and the acid or acids; examples are isopropyl formate and isopropyl acetate. The ketone may be removed with the aqueous formaldehyde solution, or, using fractional distillation, pure ketone vapour may be withdrawn at the top of the column, and the azeotropic mixture vapour lower down. In examples: (1) isopropyl ether is used in the separation of a mixture of acetic and formic acids, formaldehyde and water, and (2) isopropyl acetate is used with a mixture also containing acetone.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2219854A GB788931A (en) | 1954-07-29 | 1954-07-29 | Improvements in or relating to the separation of organic mixtures |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2219854A GB788931A (en) | 1954-07-29 | 1954-07-29 | Improvements in or relating to the separation of organic mixtures |
Publications (1)
Publication Number | Publication Date |
---|---|
GB788931A true GB788931A (en) | 1958-01-08 |
Family
ID=10175534
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2219854A Expired GB788931A (en) | 1954-07-29 | 1954-07-29 | Improvements in or relating to the separation of organic mixtures |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB788931A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5980696A (en) * | 1994-08-23 | 1999-11-09 | E. I. Du Pont De Nemours And Company | Dehydration of acetic acid by azeotropic distillation in the production of an aromatic acid |
US6150553A (en) * | 1998-08-11 | 2000-11-21 | E. I. Du Pont De Nemours And Company | Method for recovering methyl acetate and residual acetic acid in the production acid of pure terephthalic acid |
WO2001007391A1 (en) * | 1999-07-22 | 2001-02-01 | Consortium für elektrochemische Industrie GmbH | Method for separating and purifying an aqueous mixture that mainly consists of acetic acid and formic acid |
WO2001007390A1 (en) * | 1999-07-22 | 2001-02-01 | Consortium für elektrochemische Industrie GmbH | A method for the separation and purification of an aqueous mixture consisting of acetic acid and formic acid as the main components |
-
1954
- 1954-07-29 GB GB2219854A patent/GB788931A/en not_active Expired
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5980696A (en) * | 1994-08-23 | 1999-11-09 | E. I. Du Pont De Nemours And Company | Dehydration of acetic acid by azeotropic distillation in the production of an aromatic acid |
US6150553A (en) * | 1998-08-11 | 2000-11-21 | E. I. Du Pont De Nemours And Company | Method for recovering methyl acetate and residual acetic acid in the production acid of pure terephthalic acid |
WO2001007391A1 (en) * | 1999-07-22 | 2001-02-01 | Consortium für elektrochemische Industrie GmbH | Method for separating and purifying an aqueous mixture that mainly consists of acetic acid and formic acid |
WO2001007390A1 (en) * | 1999-07-22 | 2001-02-01 | Consortium für elektrochemische Industrie GmbH | A method for the separation and purification of an aqueous mixture consisting of acetic acid and formic acid as the main components |
US6695952B1 (en) | 1999-07-22 | 2004-02-24 | Consortium Fur Elektrochemische Industrie Gmbh | Method for the separation of and purification of an aqueous mixture consisting of the main components acetic acid and formic acid |
US6793777B1 (en) | 1999-07-22 | 2004-09-21 | Consortium für elektrochemische Industrie GmbH | Method for separating and purifying an aqueous mixture that mainly consists of acetic acid and formic acid |
CN1304352C (en) * | 1999-07-22 | 2007-03-14 | 电化学工业有限公司(国际) | Method for separating and purifying an aqueous mixture that mainly consists of acetic acid and formic acid |
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