GB356787A - Process for the production of concentrated aliphatic acids - Google Patents
Process for the production of concentrated aliphatic acidsInfo
- Publication number
- GB356787A GB356787A GB1463230A GB1463230A GB356787A GB 356787 A GB356787 A GB 356787A GB 1463230 A GB1463230 A GB 1463230A GB 1463230 A GB1463230 A GB 1463230A GB 356787 A GB356787 A GB 356787A
- Authority
- GB
- United Kingdom
- Prior art keywords
- acid
- column
- entraining liquid
- entraining
- liquid
- 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
- 125000001931 aliphatic group Chemical group 0.000 title abstract 2
- 239000002253 acid Substances 0.000 abstract 31
- 239000007788 liquid Substances 0.000 abstract 24
- 239000000203 mixture Substances 0.000 abstract 10
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 abstract 6
- 238000004821 distillation Methods 0.000 abstract 6
- 239000008240 homogeneous mixture Substances 0.000 abstract 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 4
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 abstract 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 abstract 2
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 abstract 2
- 239000011260 aqueous acid Substances 0.000 abstract 2
- 238000009835 boiling Methods 0.000 abstract 2
- 150000002148 esters Chemical class 0.000 abstract 2
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 abstract 2
- 150000008282 halocarbons Chemical class 0.000 abstract 2
- 239000011874 heated mixture Substances 0.000 abstract 2
- 229930195733 hydrocarbon Natural products 0.000 abstract 2
- 150000002430 hydrocarbons Chemical class 0.000 abstract 2
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 abstract 2
- DCKVNWZUADLDEH-UHFFFAOYSA-N sec-butyl acetate Chemical class CCC(C)OC(C)=O DCKVNWZUADLDEH-UHFFFAOYSA-N 0.000 abstract 2
- 239000008096 xylene Substances 0.000 abstract 2
- 150000007513 acids Chemical class 0.000 abstract 1
Classifications
-
- 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
In the concentration of acetic, propionic, butyric, and other lower acids by distilling with an added liquid (termed an entraining liquid) which forms with water an azeotropic mixture boiling at a lower temperature than the acid, the aqueous acid and the entraining liquid are brought into the form of a homogeneous mixture prior to the distillation. The dilute acid and entraining liquid may be mixed with concentrated acid, for instance they may be each introduced into the heated concentrated acid in such proportions that the mixture does not separate into layers. The dilute acid and entraining liquid may be introduced continuously into a heated mixture of concentrated acid and entraining liquid in a still, which is preferably provided with a rectifying column, and the entraining liquid which separates from the condensate is returned to the still, concentrated acid being withdrawn from the still and treated in an auxiliary distillation p column to separate anhydrous acid. Or dilute acid, entraining liquid, and concentrated acid in proportions to form a homogeneous mixture, may be introduced into a distilling column, an azeotropic mixture of water and entraining liquid passing off at the top and concentrated acid being withdrawn at the bottom without needing an auxiliary column. If desired the dilute acid, entraining liquid and concentrated acid may be mixed in a separate vessel, the mixture being withdrawn continuously and fed to a distillation column for instance at a point one-third from the bottom, an auxiliary column being unnecessary. In all cases the column may be provided with a dephlegmator or other device for returning a part of the condensate to the column, and the heat of the vapour and of the concentrated acid may be utilized for instance to heat the dilute acid and the entraining liquid. Suitable entraining liquids are hydrocarbons such as benzene or xylene, halogenated hydrocarbons such as trichlorethylene and ethylene dichloride and esters such as ethyl, propyl, and butyl acetates or mixtures of such bodies.ALSO:In the concentration of acetic, propionic, butyric and other lower aliphatic acids by distilling with an added liquid (termed an entraining liquid) which forms with water an azeotropic mixture boiling at a lower temperature than the acid, the aqueous acid and the entraining liquid are brought into the form of a homogeneous mixture prior to the distillation. The dilute acid and entraining liquid may be mixed with concentrated acid, for instance they may be each introduced into the heated concentrated acid in such proportions that the mixture does not separate into layers. The dilute acid and entraining liquid may be introduced continuously into a heated mixture of concentrated acid and entraining liquid in a still, which is preferably provided with a rectifying column, and the entraining liquid which separates from the condensate is returned to the still, concentrated acid being withdrawn from the still and treated in an auxiliary distillation column to separate anhydrous acid. Or dilute acid, entraining liquid, and concentrated acid in proportions to form a homogenous mixture, may be introduced into a distilling column, an azeotropic mixture of water and entraining liquid passing off at the top and concentrated acid being withdrawn at the bottom without needing an auxiliary column. If desired the dilute acid, entraining liquid and concentrated acid may be mixed in a separate vessel, the mixture being withdrawn continuously and fed to a distillation column, for instance at a point one third from the bottom, an auxiliary column being unnecessary. In all cases the column may be provided with a dephlegmator or other device for returning a part of the condensate to the column, and the heat of the vapour and of the concentrated acid may be utilized for instance to heat the dilute acid and/or the entraining liquid. Suitable entraining liquids are hydrocarbons such as benzene or xylene, halogenated hydrocarbons such as trichlorethylene and ethylene dichloride and esters such as ethyl, propyl and butyl acetates or mixtures of such bodies.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB1463230A GB356787A (en) | 1930-05-13 | 1930-05-13 | Process for the production of concentrated aliphatic acids |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB1463230A GB356787A (en) | 1930-05-13 | 1930-05-13 | Process for the production of concentrated aliphatic acids |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB356787A true GB356787A (en) | 1931-09-14 |
Family
ID=10044746
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB1463230A Expired GB356787A (en) | 1930-05-13 | 1930-05-13 | Process for the production of concentrated aliphatic acids |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB356787A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4661208A (en) * | 1984-11-02 | 1987-04-28 | Shin-Etsu Vinyl Acetate Co., Ltd. | Method for dehydrating distillation of an aqueous solution of carboxylic acid |
-
1930
- 1930-05-13 GB GB1463230A patent/GB356787A/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4661208A (en) * | 1984-11-02 | 1987-04-28 | Shin-Etsu Vinyl Acetate Co., Ltd. | Method for dehydrating distillation of an aqueous solution of carboxylic acid |
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