BE443894A - - Google Patents
Info
- Publication number
- BE443894A BE443894A BE443894DA BE443894A BE 443894 A BE443894 A BE 443894A BE 443894D A BE443894D A BE 443894DA BE 443894 A BE443894 A BE 443894A
- Authority
- BE
- Belgium
- Prior art keywords
- ethyl acetate
- acetic anhydride
- letter
- acetate
- please
- Prior art date
Links
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 30
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical compound CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 claims description 21
- 238000000034 method Methods 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- OPQARKPSCNTWTJ-UHFFFAOYSA-L copper(ii) acetate Chemical compound [Cu+2].CC([O-])=O.CC([O-])=O OPQARKPSCNTWTJ-UHFFFAOYSA-L 0.000 claims description 3
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 2
- 239000003054 catalyst Substances 0.000 claims description 2
- 229910001882 dioxygen Inorganic materials 0.000 claims description 2
- 229910052751 metal Inorganic materials 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- 150000003839 salts Chemical class 0.000 claims description 2
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 claims 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 10
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 8
- KFSLWBXXFJQRDL-UHFFFAOYSA-N Peracetic acid Chemical compound CC(=O)OO KFSLWBXXFJQRDL-UHFFFAOYSA-N 0.000 description 6
- 230000017105 transposition Effects 0.000 description 6
- 150000008064 anhydrides Chemical class 0.000 description 5
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 3
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229940011182 cobalt acetate Drugs 0.000 description 2
- QAHREYKOYSIQPH-UHFFFAOYSA-L cobalt(II) acetate Chemical compound [Co+2].CC([O-])=O.CC([O-])=O QAHREYKOYSIQPH-UHFFFAOYSA-L 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 150000004965 peroxy acids Chemical class 0.000 description 2
- HHDMWMVEWGHCJO-UHFFFAOYSA-J C(C)(=O)[O-].[Co+2].[Cu+2].C(C)(=O)[O-].C(C)(=O)[O-].C(C)(=O)[O-] Chemical compound C(C)(=O)[O-].[Co+2].[Cu+2].C(C)(=O)[O-].C(C)(=O)[O-].C(C)(=O)[O-] HHDMWMVEWGHCJO-UHFFFAOYSA-J 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000001838 alkalimetric titration Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 229940071125 manganese acetate Drugs 0.000 description 1
- UOGMEBQRZBEZQT-UHFFFAOYSA-L manganese(2+);diacetate Chemical compound [Mn+2].CC([O-])=O.CC([O-])=O UOGMEBQRZBEZQT-UHFFFAOYSA-L 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000006462 rearrangement reaction Methods 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 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
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/23—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of oxygen-containing groups to carboxyl groups
- C07C51/235—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of oxygen-containing groups to carboxyl groups of —CHO groups or primary alcohol groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/54—Preparation of carboxylic acid anhydrides
- C07C51/56—Preparation of carboxylic acid anhydrides from organic acids, their salts, their esters or their halides, e.g. by carboxylation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Description
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procédé pour la fabrication d'anhydride acétique.
La manière d'obtenir directement de l'anhydride acétique par oxydation d'acétate d'éthyle au moyen d'oxygène moléculaire est déjà connue.
Il a été trouvé récemment que, partant d'éther d'acide per- acétique produit à basse température, on obtenait aussi à une température légèrement supérieure, par décomposition spontanée, de l'anhydride acétique. L'obtention d'éther d'acide peracétique se fait par exemple de la manière décrite dans le brevet allemand (demande du 23 Décembre 1940)pour: "Procédé pour la fabrication de percombinaisons", où l'acétate d'éthyle décomposé est à peu près quantitativement transformé en éther de peracide. Dans la réaction de transposition, il se forme de l'anhydride acétique et de l'eau, en même temps que de l'acide acétique. La formation d'anhydride est favorisée par la présence d'un sel métallique, en particulier d'acétate de cuivre, agissant comme catalyseur.
Lors de la réaction de transposition, le rendement en anhydride est encore amélioré lorsque la solution d'éther du @
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peracide contient de l'acétate d'éthyle libre. L'aldéhyde en excès peut être libérée séparément lors de la réaction de transposition ou bien, lors de la préparation du peréther; une partie seulement de l'aldéhyde introduite est oxydée. Il s'agit ici manifestement de l'action d'un agent intermédiaire.
Un des avantages du nouveau procédé réside en ce qu'il est possible d'obtenir un bon rendement en anhydride sans utiliser un appareil à pression.
Exemple 1.
Une solution d'éther d'acide peracétique, obtenue par oxyda- tion complète d'une solution de 16 gr. d'acétate d'éthyle dans 40'gr. d'acide acétique cristallisable, avec addition de 0,5% de son poids d'acétate de cobalt, au moyen d'oxygène sec à 0 , jusqu'à absorption d'environ 0,5 molécule gramme d'oxygène par molé.gr. d'acétate d'éthyle, est échauffée lentement afin d'amener la trans- position. La fin de la réaction a pu être facilement fixée par la diminution de la quantité de chaleur développée et de la teneur en peréther.
Immédiatement après, l'anhydride formé est déterminée par titration alcalimétrique avec ou sans aniline, partant du peréther formé, le rendement atteignait 12 % rapporté à la quantité théoriquement possible lors d'une décomposition quantitative en anhydride et eau.
Exemple 2.
Le processus de fabrication est le même due celui de l'exemple 1, avec cependant comme différence due, lors de la réaction de transposition, la même quantité d'acétate de cuivre est ajoutée à l'acétate de cobalt déjà utilisé. Le rendement atteignit 38
Exemple
En procédant comme dans l'exemple 1, mais en ajoutant 0,5% d'acétate de manganèse lors de la réaction de transposition, le rendement obtenu a été de 30 %.
Exemple 4.
De l'acétate d'éthyle (20 - 40 gr.) en excès est ajouté, en tant qu'agent intermédiaire influençant la réaction, à la solution de peréther constituée suivant l'exemple 1, et la réaction de - @
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transposition est réalisée en présence d'acétate de cuivre-cobalt (0,3 gr. de chacun d'eux). Le rendement calculé sur l'aldéhyde oxydée atteignit 60
Exemple 5.
Une solution de 16 gr. d'acétate d'éthyle dans 15 gr. d'acide acétique cristallisable fut oxydée lentement jusqu'à concurrence de la moitié, puis décomposée comme dans l'exemple 4. Le rendement calculé sur l'aldéhyde oxydée atteignit environ 72 %.
L'anhydride acétique, précipitant dans les mélanges de décomposition, peut être retiré à l'état pur, suivant des méthodes connues, par exemple celles décrites dans les brevets allemands N 411.106 et N 511.195, en excluant à peu près complètement toute hydratation par l'eau de réaction.
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process for the manufacture of acetic anhydride.
The manner of obtaining acetic anhydride directly by oxidation of ethyl acetate by means of molecular oxygen is already known.
It has recently been found that, starting from ether of peracetic acid produced at low temperature, acetic anhydride is also obtained at a slightly higher temperature by spontaneous decomposition. The peracetic acid ether is obtained, for example, in the manner described in the German patent (application of December 23, 1940) for: "Process for the manufacture of percombinations", where the decomposed ethyl acetate is at roughly quantitatively converted to peracid ether. In the transposition reaction, acetic anhydride and water are formed, along with acetic acid. The formation of anhydride is favored by the presence of a metal salt, in particular copper acetate, acting as a catalyst.
During the rearrangement reaction, the yield of anhydride is further improved when the ether solution of @
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peracid contains free ethyl acetate. The excess aldehyde can be released separately during the transposition reaction or else during the preparation of the perether; only part of the introduced aldehyde is oxidized. This is clearly the action of an intermediary agent.
One of the advantages of the new process is that it is possible to obtain a good yield of anhydride without using a pressure vessel.
Example 1.
A solution of peracetic acid ether, obtained by complete oxidation of a solution of 16 gr. of ethyl acetate in 40'gr. of crystallizable acetic acid, with the addition of 0.5% of its weight of cobalt acetate, by means of dry oxygen at 0, until absorption of approximately 0.5 gram molecule of oxygen per mol. . of ethyl acetate, is slowly heated in order to bring about the transposition. The end of the reaction could be easily fixed by the decrease in the amount of heat developed and in the perether content.
Immediately afterwards, the anhydride formed is determined by alkalimetric titration with or without aniline, starting from the perether formed, the yield reached 12% relative to the theoretically possible amount during a quantitative decomposition into anhydride and water.
Example 2.
The manufacturing process is the same due to that of Example 1, with the difference, however, that during the transposition reaction, the same quantity of copper acetate is added to the cobalt acetate already used. The yield reached 38
Example
By proceeding as in Example 1, but adding 0.5% of manganese acetate during the transposition reaction, the yield obtained was 30%.
Example 4.
Ethyl acetate (20 - 40 gr.) In excess is added, as an intermediate influencing the reaction, to the perether solution formed according to Example 1, and the reaction of - @
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transposition is carried out in the presence of copper-cobalt acetate (0.3 gr. of each of them). The calculated yield on the oxidized aldehyde reached 60
Example 5.
A solution of 16 gr. of ethyl acetate in 15 gr. Crystallizable acetic acid was slowly oxidized to half and then decomposed as in Example 4. The calculated yield on the oxidized aldehyde was about 72%.
Acetic anhydride, which precipitates in decomposition mixtures, can be removed in the pure state, according to known methods, for example those described in German Patents Nos. 411,106 and N 511,195, almost completely excluding any hydration by the water of reaction.
Claims (1)
Publications (1)
| Publication Number | Publication Date |
|---|---|
| BE443894A true BE443894A (en) |
Family
ID=100703
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| BE443894D BE443894A (en) |
Country Status (1)
| Country | Link |
|---|---|
| BE (1) | BE443894A (en) |
-
0
- BE BE443894D patent/BE443894A/fr unknown
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