CH324667A - Process for the production of vinyl esters of organic acids - Google Patents
Process for the production of vinyl esters of organic acidsInfo
- Publication number
- CH324667A CH324667A CH324667DA CH324667A CH 324667 A CH324667 A CH 324667A CH 324667D A CH324667D A CH 324667DA CH 324667 A CH324667 A CH 324667A
- Authority
- CH
- Switzerland
- Prior art keywords
- vinyl esters
- acid
- production
- organic acids
- acids
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 9
- 229920001567 vinyl ester resin Polymers 0.000 title claims description 7
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 title claims description 7
- 238000004519 manufacturing process Methods 0.000 title claims description 3
- 235000005985 organic acids Nutrition 0.000 title description 5
- 150000007524 organic acids Chemical class 0.000 title description 4
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical compound CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 claims description 9
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 claims description 7
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 claims description 7
- 125000004432 carbon atom Chemical group C* 0.000 claims description 6
- 239000002253 acid Substances 0.000 claims description 5
- 150000001244 carboxylic acid anhydrides Chemical class 0.000 claims description 5
- 239000003054 catalyst Substances 0.000 claims description 5
- 150000001735 carboxylic acids Chemical class 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- 150000007513 acids Chemical class 0.000 claims description 3
- WYVAMUWZEOHJOQ-UHFFFAOYSA-N propionic anhydride Chemical compound CCC(=O)OC(=O)CC WYVAMUWZEOHJOQ-UHFFFAOYSA-N 0.000 claims description 2
- 239000000654 additive Substances 0.000 claims 2
- 230000000996 additive effect Effects 0.000 claims 2
- 238000007792 addition Methods 0.000 claims 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- ZEYHEAKUIGZSGI-UHFFFAOYSA-N 4-methoxybenzoic acid Chemical compound COC1=CC=C(C(O)=O)C=C1 ZEYHEAKUIGZSGI-UHFFFAOYSA-N 0.000 description 4
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 4
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 239000007858 starting material Substances 0.000 description 3
- UOBYKYZJUGYBDK-UHFFFAOYSA-N 2-naphthoic acid Chemical compound C1=CC=CC2=CC(C(=O)O)=CC=C21 UOBYKYZJUGYBDK-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000005711 Benzoic acid Substances 0.000 description 2
- 235000021314 Palmitic acid Nutrition 0.000 description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 2
- 235000010233 benzoic acid Nutrition 0.000 description 2
- 150000001661 cadmium Chemical class 0.000 description 2
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- IPCSVZSSVZVIGE-UHFFFAOYSA-N hexadecanoic acid Chemical compound CCCCCCCCCCCCCCCC(O)=O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 description 2
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 2
- 229910052753 mercury Inorganic materials 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000011541 reaction mixture Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910052725 zinc Inorganic materials 0.000 description 2
- 239000011701 zinc Substances 0.000 description 2
- 239000011787 zinc oxide Substances 0.000 description 2
- LNETULKMXZVUST-UHFFFAOYSA-N 1-naphthoic acid Chemical compound C1=CC=C2C(C(=O)O)=CC=CC2=C1 LNETULKMXZVUST-UHFFFAOYSA-N 0.000 description 1
- IKCLCGXPQILATA-UHFFFAOYSA-N 2-chlorobenzoic acid Chemical compound OC(=O)C1=CC=CC=C1Cl IKCLCGXPQILATA-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- AAYFQAPISKPSSI-UHFFFAOYSA-N [N].C#C Chemical compound [N].C#C AAYFQAPISKPSSI-UHFFFAOYSA-N 0.000 description 1
- 159000000032 aromatic acids Chemical class 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- UJRIYYLGNDXVTA-UHFFFAOYSA-N ethenyl hexadecanoate Chemical compound CCCCCCCCCCCCCCCC(=O)OC=C UJRIYYLGNDXVTA-UHFFFAOYSA-N 0.000 description 1
- BGVWGPMAGMJLBU-UHFFFAOYSA-N ethenyl naphthalene-1-carboxylate Chemical compound C1=CC=C2C(C(=O)OC=C)=CC=CC2=C1 BGVWGPMAGMJLBU-UHFFFAOYSA-N 0.000 description 1
- 238000004508 fractional distillation Methods 0.000 description 1
- WQEPLUUGTLDZJY-UHFFFAOYSA-N n-Pentadecanoic acid Natural products CCCCCCCCCCCCCCC(O)=O WQEPLUUGTLDZJY-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- 150000002943 palmitic acids Chemical class 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- KOZCZZVUFDCZGG-UHFFFAOYSA-N vinyl benzoate Chemical compound C=COC(=O)C1=CC=CC=C1 KOZCZZVUFDCZGG-UHFFFAOYSA-N 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Description
Verfahren zur Herstellung von Vinylestern organischer Säuren Vinylester organischer Säuren werden meist durch Einwirkung von Azetylen auf die organischen Säuren in Gegenwart von Queck- silber-, Zink- oder Cadmiiunsalzen hergestellt. Die Reaktion lässt sich leicht durchführen mit niederen organischen Säuren, wie z. B. Essig säure, dagegen bietet sie Schwierigkeiten bei der Verwendung von höheren Säuren, die mehr als 6 C-Atome im Molekül enthalten.
Durch Anwesenheit geringerer Mengen von Wasser, z. B. 0,5-2 /o-, wie sie in den tech nisch reinen Säuren meistens enthalten sind, werden die gebildeten Vinylester sofort wieder hy drolysiert und man erhält neben der unver änderten Säure braune undefinierbare Neben produkte. Bekanntlich ist es umständlich und oft sehr schwierig, die letzten Reste an Wasser aus den Ausgangsstoffen zu entfernen. Gemäss der Arbeitsweise der Erfindung ist nun dies nicht nötig.
Gegenstand vorliegenden Patentes ist ein Verfahren zur Herstellung von Vinylestern durch Umsetzung organischer Carbonsäuren mit mehr als 6 C-Atomen im iVTolekül mit Azetylen durch Erhitzen in Gegenwart von Katalysatoren, das dadurch gekennzeichnet ist, dass man die Umsetzung noch in Gegen wart von Carbonsäureanhydriden durchführt.
Als Carbonsäuren mit mehr als 6 C-Atomen im Molekül kommen zum Beispiel Palmitin- säuren, Stearinsäure oder insbesondere aroma tische Säuren, wie Benzoesäure, Anissäure, a- oder ss-Naphthoesäure, oder Chlorbenzoe- säure in Betracht.
Als Carbonsäureanhydride mit weniger als 4 C-Atomen im Säuremolekül eignen sich zum Beispiel Essigsäure- oder Propionsäureanhydrid.
Die Menge des zugesetzten Carbonsäure- anhydrids richtet sich nach dem Feuchtig keitsgehalt der Ausgangsmaterialien und kann zwischen 1 und etwa 5' /o der verwendeten Carbonsäure schwanken. In manchen Fällen ist die Anwendung grösserer Mengen zweck mässig. Durch diese Arbeitsweise erübrigt sich, wie bereits dargelegt, die umständliche Trock nung -der Ausgangsprodukte, und es werden im allgemeinen sehr gute Ausbeuten erzielt.
Die Herstellung der Vinylester erfolgt nach den bekannten Bedingungen durch Er hitzen der Carbonsäure mit Azetylen in Gegen wart von Katalysatoren, wie z. B. Quecksilber-, Zink- oder Cadmiumsalzen der entsprechen den Carbonsäuren. Die genannten- Salze kann man gegebenenfalls auch im Reaktionsgemisch durch Zugabe der entsprechenden Oxyde er zeugen.
Beispiel <I>2</I> In 100 Gewichtsteile technischer reiner Palmitinsäure werden 1,5 Gewichtsteile Zink oxyd unter Erwärmen aufgelöst und nach Zu gabe von 3 Gewichtsteilen Essigsätireanhydrid das Reaktionsgemisch in einem Rührautokla- ven mit einem Gemisch von Azetylen und Stickstoff im Verhältnis 2: 1 bei 10-20 Atm. Überdruck auf 175 C bis zur Beendigung der Azetylenaufnahme erhitzt. Das verbrauchte Azetylen wird jeweils durch Nachdrücken ergänzt.
Das Reaktionsprodukt wird mit Benzol verdünnt, der abgeschiedene Katalysa tor abfiltriert und das Filtrat durch frak tionierte Destillation gereinigt. Die Ausbeute an Vinylpalmitat ist fast quantitativ.
<I>Beispiel</I> 500 Gewichtsteile Benzoesäure werden mit 2 Gewichtsteilen Zinkoxyd bis zur klaren Schmelze zusamxriengeschmolzen und nach dein Zusatz von 100 Gewichtsteilen Essigsäure anhydrid und 500 Gewichtsteilen xylol in einem Autoklaven mit einem Azetylen-Stick- stoff-Gemiseh im Verhältnis 1 :1 bei 180 bis l85 C und 20 Atm. bis zur Druckkonstanz erhitzt.
Der ausgeschiedene Katalysator wird nach dem Abkühlen abfiltriert und das Fil trat fraktioniert destilliert, wobei man mit 80 o/oiger ausbeute Vinylbenzoat erhält.
In gleicher Weise erhält man aus 500 Ge wichtsteilen Anissäure etwa 400 Gewichtsteile Vinylanisoat und aus ss-Naphthoesäure das Vinylnaphthoat.
Process for the production of vinyl esters of organic acids Vinyl esters of organic acids are mostly produced by the action of acetylene on the organic acids in the presence of mercury, zinc or cadmium salts. The reaction can be easily carried out with lower organic acids, such as. B. acetic acid, however, it presents difficulties when using higher acids that contain more than 6 carbon atoms in the molecule.
By the presence of smaller amounts of water, e.g. B. 0.5-2 / o, as they are usually contained in the technically pure acids, the vinyl esters formed are immediately hydrolyzed again and you get brown undefinable by-products in addition to the unchanged acid. It is known that it is cumbersome and often very difficult to remove the last remnants of water from the starting materials. According to the method of operation of the invention, this is not necessary.
The present patent relates to a process for the preparation of vinyl esters by reacting organic carboxylic acids having more than 6 carbon atoms in the molecule with acetylene by heating in the presence of catalysts, which is characterized in that the reaction is carried out in the presence of carboxylic anhydrides.
Possible carboxylic acids with more than 6 carbon atoms in the molecule are, for example, palmitic acids, stearic acid or, in particular, aromatic acids, such as benzoic acid, anisic acid, α- or β-naphthoic acid, or chlorobenzoic acid.
Suitable carboxylic acid anhydrides with fewer than 4 carbon atoms in the acid molecule are, for example, acetic acid or propionic acid anhydride.
The amount of added carboxylic anhydride depends on the moisture content of the starting materials and can vary between 1 and about 5% of the carboxylic acid used. In some cases it is advisable to use larger amounts. As already explained, this procedure obviates the need for the laborious drying of the starting materials, and very good yields are generally achieved.
The vinyl esters are prepared according to the known conditions by heating the carboxylic acid with acetylene in the presence of catalysts such as. B. mercury, zinc or cadmium salts correspond to the carboxylic acids. The salts mentioned can optionally also be generated in the reaction mixture by adding the corresponding oxides.
Example <I> 2 </I> In 100 parts by weight of technical grade palmitic acid, 1.5 parts by weight of zinc oxide are dissolved with heating and, after adding 3 parts by weight of acetic anhydride, the reaction mixture is placed in a stirred autoclave with a mixture of acetylene and nitrogen in a ratio of 2 : 1 at 10-20 atm. Overpressure heated to 175 C until the end of the acetylene uptake. The acetylene consumed is supplemented in each case by pressing.
The reaction product is diluted with benzene, the deposited catalyst is filtered off and the filtrate is purified by fractional distillation. The vinyl palmitate yield is almost quantitative.
<I> Example </I> 500 parts by weight of benzoic acid are melted together with 2 parts by weight of zinc oxide to a clear melt and, after adding 100 parts by weight of acetic anhydride and 500 parts by weight of xylene, in an autoclave with an acetylene-nitrogen mixture in a ratio of 1: 1 at 180 to 185 C and 20 Atm. heated to constant pressure.
After cooling, the precipitated catalyst is filtered off and the filtrate is fractionally distilled, giving vinyl benzoate with an 80% yield.
In the same way, about 400 parts by weight of vinyl anisoate are obtained from 500 parts by weight of anisic acid, and vinyl naphthoate is obtained from β-naphthoic acid.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH324667T | 1954-01-14 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CH324667A true CH324667A (en) | 1957-10-15 |
Family
ID=4499621
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CH324667D CH324667A (en) | 1954-01-14 | 1954-01-14 | Process for the production of vinyl esters of organic acids |
Country Status (1)
| Country | Link |
|---|---|
| CH (1) | CH324667A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1204657B (en) * | 1960-08-30 | 1965-11-11 | Distillers Co Yeast Ltd | Process for the production of vinyl esters |
| DE1237557B (en) * | 1962-07-10 | 1967-03-30 | Shell Int Research | Process for the preparation of vinyl esters of saturated aliphatic monocarboxylic acids |
| US7982065B2 (en) | 2009-05-07 | 2011-07-19 | Celanese International Corporation | Vinyl ester production from acetylene and carboxylic acid utilizing heterogeneous catalyst |
| US8173830B2 (en) | 2009-05-07 | 2012-05-08 | Celanese International Corporation | Vinyl ester production from acetylene and carboxylic acid utilizing homogeneous catalyst |
-
1954
- 1954-01-14 CH CH324667D patent/CH324667A/en unknown
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1204657B (en) * | 1960-08-30 | 1965-11-11 | Distillers Co Yeast Ltd | Process for the production of vinyl esters |
| DE1237557B (en) * | 1962-07-10 | 1967-03-30 | Shell Int Research | Process for the preparation of vinyl esters of saturated aliphatic monocarboxylic acids |
| US7982065B2 (en) | 2009-05-07 | 2011-07-19 | Celanese International Corporation | Vinyl ester production from acetylene and carboxylic acid utilizing heterogeneous catalyst |
| US8173830B2 (en) | 2009-05-07 | 2012-05-08 | Celanese International Corporation | Vinyl ester production from acetylene and carboxylic acid utilizing homogeneous catalyst |
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