GB307868A - Process and apparatus for the continuous extraction of acetic acid from its aqueous solutions - Google Patents
Process and apparatus for the continuous extraction of acetic acid from its aqueous solutionsInfo
- Publication number
- GB307868A GB307868A GB16186/28A GB1618628A GB307868A GB 307868 A GB307868 A GB 307868A GB 16186/28 A GB16186/28 A GB 16186/28A GB 1618628 A GB1618628 A GB 1618628A GB 307868 A GB307868 A GB 307868A
- Authority
- GB
- United Kingdom
- Prior art keywords
- vessels
- delivered
- mixing
- acetic acid
- pipes
- 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
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 title abstract 11
- 239000007864 aqueous solution Substances 0.000 title abstract 3
- 238000000605 extraction Methods 0.000 title abstract 3
- 238000000034 method Methods 0.000 title 1
- 239000000243 solution Substances 0.000 abstract 5
- 239000002904 solvent Substances 0.000 abstract 4
- 229940072049 amyl acetate Drugs 0.000 abstract 2
- PGMYKACGEOXYJE-UHFFFAOYSA-N anhydrous amyl acetate Natural products CCCCCOC(C)=O PGMYKACGEOXYJE-UHFFFAOYSA-N 0.000 abstract 2
- 229920002301 cellulose acetate Polymers 0.000 abstract 2
- MNWFXJYAOYHMED-UHFFFAOYSA-M heptanoate Chemical compound CCCCCCC([O-])=O MNWFXJYAOYHMED-UHFFFAOYSA-M 0.000 abstract 2
- 239000007788 liquid Substances 0.000 abstract 2
- 238000000926 separation method Methods 0.000 abstract 2
- 239000007787 solid Substances 0.000 abstract 2
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 238000004140 cleaning Methods 0.000 abstract 1
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical compound O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 abstract 1
- 239000000284 extract Substances 0.000 abstract 1
- 239000012530 fluid Substances 0.000 abstract 1
- 230000005484 gravity Effects 0.000 abstract 1
- 238000002347 injection Methods 0.000 abstract 1
- 239000007924 injection Substances 0.000 abstract 1
- 238000007689 inspection Methods 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 239000000126 substance Substances 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
- C07C51/48—Separation; Purification; Stabilisation; Use of additives by liquid-liquid treatment
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Extraction Or Liquid Replacement (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
307,868. Soc. Anon. des Distilleries des Deux-Sevres. March 15, 1928, [Convention date]. Extracts, making.- Acetic acid is extracted from aqueous solutions thereof, for example solutions obtained in the manufacture of cellulose acetate, by passing the solution, in countercurrent to an extracting medium such as amyl acetate, through multistage apparatus, each stage of which comprises a mixer, in which the two phases are thoroughly emulsified, and a settling vessel in which they are allowed to separate, the enriched extraction medium being then passed to the one and the solvent to the other adjacent stage. The apparatus may be carried out at temperatures above or below atmospheric temperatures and at pressures greater or less than normal. The stages of the apparatus may be arranged in one or more rows, in circular formation, or the mixing and settling elements may be superposed to form two towers or may be combined into a single tower. Circulation of the fluids may be effected by pumps, by compressed gas or, as regards one of the phases, by gravity. The mixing apparatus may be made to serve as a pump for this purpose. As illustrated, the apparatus comprises mixing vessels M1 - - M5 and settling vessels D1 - - D5. The solution to be extracted, for example a 10 per cent aqueous solution of acetic acid, is delivered to mixer M5 through a pipe 34 and the extracting medium M1 through a pipe 36. The liquids pass in opposite directions through the apparatus, being at each stage thoroughly emulsified in the mixing vessels' and then delivered to the separating vessels. After separation the upper layer containing amyl acetate enriched with acetic acid is passed through pipes such as 10, 22 to the next lower mixing vessel and the lower layer is delivered through vessels G1 - - G5 and pipes such as 23, 24, 27 to the next higher mixing vessel. Delivery of the lower layer is effected by the injection action of compressed air supplied through pipes 25 from a reservoir 26. The used air is trapped in vessels HI - - H5 and delivered through pipes 28, 29 to a reservoir 30 whence it is returned in compressed condition to the reservoir 26 by a pump 31. The extractladen solvent is delivered from the apparatus by a pipe 33 and the extracted solution by a pipe 35. Where the solution contains precipitatable solid matter such as cellulose acetate this solid matter remains at the top or bottom of the setting vessels or at the surface of separation of the two liquids and may be removed as by periodical cleaning of the vessels. The Specification as open to inspection under Sect. 91 (3) (a) describes the invention as applicable to the extraction in general of substances dissolved in solvents, by means of extracting media insoluble or substantially insoluble in the solvent. This subject-matter does not appear in the Specification as accepted.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| BE307868X | 1928-03-15 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB307868A true GB307868A (en) | 1929-11-04 |
Family
ID=3867508
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB16186/28A Expired GB307868A (en) | 1928-03-15 | 1928-06-02 | Process and apparatus for the continuous extraction of acetic acid from its aqueous solutions |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB307868A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2220151A (en) * | 1988-04-18 | 1990-01-04 | Nitrokemia Ipartelepek | Countercurrent extraction |
| GB2223959A (en) * | 1988-09-12 | 1990-04-25 | First Chemical Corp | Recovering nitrophenolic by-products. |
-
1928
- 1928-06-02 GB GB16186/28A patent/GB307868A/en not_active Expired
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2220151A (en) * | 1988-04-18 | 1990-01-04 | Nitrokemia Ipartelepek | Countercurrent extraction |
| GB2223959A (en) * | 1988-09-12 | 1990-04-25 | First Chemical Corp | Recovering nitrophenolic by-products. |
| GB2223959B (en) * | 1988-09-12 | 1992-05-13 | First Chemical Corp | Treatment of nitrophenolic by-products |
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