DE832291C - Process for the preparation of ª † -oxybutyraldehyde - Google Patents
Process for the preparation of ª † -oxybutyraldehydeInfo
- Publication number
- DE832291C DE832291C DEB2126A DEB0002126A DE832291C DE 832291 C DE832291 C DE 832291C DE B2126 A DEB2126 A DE B2126A DE B0002126 A DEB0002126 A DE B0002126A DE 832291 C DE832291 C DE 832291C
- Authority
- DE
- Germany
- Prior art keywords
- butanediol
- cobalt
- oxybutyraldehyde
- preparation
- copper
- 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
- 238000000034 method Methods 0.000 title claims description 4
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 claims description 12
- 239000003054 catalyst Substances 0.000 claims description 9
- 229910017052 cobalt Inorganic materials 0.000 claims description 7
- 239000010941 cobalt Substances 0.000 claims description 7
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 3
- YEJRWHAVMIAJKC-UHFFFAOYSA-N 4-Butyrolactone Chemical compound O=C1CCCO1 YEJRWHAVMIAJKC-UHFFFAOYSA-N 0.000 description 8
- CDQSJQSWAWPGKG-UHFFFAOYSA-N butane-1,1-diol Chemical compound CCCC(O)O CDQSJQSWAWPGKG-UHFFFAOYSA-N 0.000 description 5
- 229910052802 copper Inorganic materials 0.000 description 5
- 239000010949 copper Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 229930188620 butyrolactone Natural products 0.000 description 4
- 238000006356 dehydrogenation reaction Methods 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- RYTYSMSQNNBZDP-UHFFFAOYSA-N cobalt copper Chemical compound [Co].[Cu] RYTYSMSQNNBZDP-UHFFFAOYSA-N 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 3
- 239000000741 silica gel Substances 0.000 description 3
- 229910002027 silica gel Inorganic materials 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000011541 reaction mixture Substances 0.000 description 2
- 229910052596 spinel Inorganic materials 0.000 description 2
- 239000011029 spinel Substances 0.000 description 2
- -1 B. copper Chemical class 0.000 description 1
- 241000605059 Bacteroidetes Species 0.000 description 1
- 241000530268 Lycaena heteronea Species 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 150000001868 cobalt Chemical class 0.000 description 1
- UFMZWBIQTDUYBN-UHFFFAOYSA-N cobalt dinitrate Chemical compound [Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O UFMZWBIQTDUYBN-UHFFFAOYSA-N 0.000 description 1
- 229910001981 cobalt nitrate Inorganic materials 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 229910052566 spinel group Inorganic materials 0.000 description 1
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
- C07C45/002—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by dehydrogenation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Verfahren zur Herstellung von y-Oxybutyraldehyd Es ist bereits bekannt, 1, 4-Butandiol durch Erhitzen in Gegenwart von Katalysatoren zu dehydrieren. Die bisher hierzu verwendeten Dehydrierungskatalysatoren, vorzugsweise Kupfer, gewisse Metalle der B. Gruppe und oxydische Katalysatoren, führen die Reaktion so, daß Butyrolacton das Hauptdehydrierungsprodukt ist, während der auf einer niedrigeren Oxydationsstufe stehende y-Oxybutyraldellyd nicht oder nur in sehr untergeordneter Menge gebildet wird. Da ;,-Oxyl>utyraldehvd und Butvrolacton überdies sich nicht sehr einfach trennen lassen, waren die bisher bekannten Dehydrierungsmethoden für 1, 4-Butandiol zur 1-lerstellung dieses Aldehyds kaum brauchbar.Process for the production of y-oxybutyraldehyde It is already known To dehydrate 1,4-butanediol by heating in the presence of catalysts. the dehydrogenation catalysts previously used for this purpose, preferably copper, certain Metals of the B. group and oxidic catalysts lead the reaction in such a way that butyrolactone is the major dehydrogenation product, while that at a lower level of oxidation standing y-oxybutyraldellyd not formed or only in a very minor amount will. Since;, - Oxyl> utyraldehvd and butvrolactone, moreover, do not separate very easily let, were the previously known dehydrogenation methods for 1, 4-butanediol for 1-l production of this aldehyde hardly usable.
Es wurde nun gefunden, daß die Dehydrierung des 1, 4-Butandiols einen anderen Verlauf nimmt und man als Produkt vorzugsweise den ;,-Oxyl>utyraldehyd erhält, wenn man Kobaltkatalysatoren, insbesondere solche, deren katalytisch wirksamer Anteil überwiegend aus Kobalt besteht, verwendet. Man kann metallisches Kobalt als solches, gegebenenfalls auf Trägern, wie Kieselgel, verwenden; besonders geeignet sind Trägerkatalysatoren, die durch Tränken mit einer Kobaltsalzlösung, z. B. Kobaltnitrat, und Reduktion bei Temperaturen unter 20o° hergestellt wurden. Durch andere Metalle, z. B. Kupfer, kann das Kobalt noch aktiviert werden. Hervorragend haben sich reduzierte synthetische Kobaltkupferspinelle bewährt, die nahezu butyrolactonfreien y-Oxybutyraldehyd liefern. Die Dehydrierung wird am einfachsten bei gewöhnlichem Druck bzw. in einer indifferenten Atmosphäre, wie in Gegenwart von Stickstoff oder Wasserstoff, im allgemeinen bei Temperaturen zwischen 15o und 300° ausgeführt. Zweckmäßig wählt man die Temperatur zwischen 19o und 2300. 1)1e besten Ausbeuten erhält man, wenn man wasserfreies oder wasserarmes, vorzugsweise unter 5 % «'asser enthaltendes Butandiol benutzt und den Durchsatz so wählt, daß nicht mehr als etwa die Hälfte, besser nicht über 40%, umgesetzt werden.It has now been found that the dehydrogenation of 1, 4-butanediol one takes a different course and the product preferably obtained is;, - oxyl> utyraldehyde, when using cobalt catalysts, especially those whose catalytically active part consists predominantly of cobalt, is used. Metallic cobalt can be used as such, optionally use on supports such as silica gel; supported catalysts are particularly suitable, by soaking with a cobalt salt solution, e.g. B. Cobalt Nitrate, and Reduction were produced at temperatures below 20o °. By other metals, e.g. B. copper, the cobalt can still be activated. Reduced synthetic ones have proven to be excellent Tried and tested cobalt copper spinels, which provide almost butyrolactone-free γ-oxybutyraldehyde. Dehydration is easiest at ordinary pressure or in an indifferent one Atmosphere, such as in the presence of nitrogen or hydrogen, in general Temperatures executed between 15o and 300 °. Appropriately chooses the temperature is between 19o and 2300. 1) 1e best yields are obtained if anhydrous or low-water butanediol, preferably less than 5% water, is used used and the throughput selected so that no more than about half, better not over 40% are implemented.
Der gebildete y-Oxyl>utyraldehyd kann aus dem nicht verbrauchten Butandiol durch Destillation abgetrieben werden. Das zurückbleibende Butandiol kann man erneut der Reaktion zuführen. 'Man kann auch das Reaktionsgemisch mit der gleichen Menge \Vasser verdünnen und durch Extraktion mit organischen Lösungsmitteln, wie z. B. Äther, den Aldehyd isolieren oder den y-Oxybutyraldehyd mit Wasserdampf abtreiben, wobei man ein sehr reines Produkt erhält. Beispiel i Durch ein Rohr von o,85 m Länge ulid 3o mm Durchmesser, das mit 750 cm3 eines auf Kies21ge1 aufgetragenen Kobaltkatalysators (Co-Gehalt 200/0) beschickt ist, leitet man stündlich 6o em3 reines 1, 4-Butandiol in schwachem Stickstoffstrom bei 195'. Das Reaktionsgemisch, das aus dem Rohr abzieht, enthält 28% y-Oxybutyraldehyd und 0,5% Butyrolacton, der Rest ist Butandiol. Durch einmaliges Destillieren erhält man einen 8o%igen y-Oxyl>utyraldehyd; er kann duroli eine zweite Destillation weiter konzentriert werden.The γ-oxyl> utyraldehyde formed can be driven off from the unused butanediol by distillation. The remaining butanediol can be fed back into the reaction. 'You can also dilute the reaction mixture with the same amount of water and extract it with organic solvents, such as. B. ether, isolate the aldehyde or drive off the y-oxybutyraldehyde with steam, whereby a very pure product is obtained. EXAMPLE i 60 cubic meters of pure 1,4-butanediol are passed hourly through a tube 0.85 m long and 30 mm in diameter, which is charged with 750 cm3 of a cobalt catalyst (Co content 200/0) applied to Kies21ge1 at 195 '. The reaction mixture withdrawn from the tube contains 28% γ-oxybutyraldehyde and 0.5% butyrolactone, the remainder being butanediol. A single distillation gives an 80% γ-oxyl>utyraldehyde; it can be further concentrated duroli a second distillation.
Verwendet man unter sonst gleichen Bedingungen bei i gor einen aus Kobalt und Kupfer auf Kieselgel (20% Co, 1 % Cu) bestehenden, bei 17o° in schwachem Wasserstoffstrcm reduzierten Katalysator, so werden 33 bis 35% des 13tttandiols in y-Oxy~butyraldelivd verwandelt. Der Gehalt des Produktes an 13titvrolactc»i beträgt o,80/0. 13eisl)iel 2 Über 75o cm3 eines atis Kobaltkupferspinell auf Kieselgel bestehenden Katalysators (16,2% Co, 8,8% Cu), der bei 40o° im Wasserstoffstrom reduziert wurde, leitet man stündlich hei 225° 6o cin3 reines i, 4-Butandiol im Gemisch mit Stickstoff. Das i, 4-Butandiol wird zu 40% in y-Oxyliutyraldehyd umgesetzt. plan treibt aus dem Reaktionsprodukt den y-Oxybutyral(leliyd mit Wasserdampf ab, äthert das Kondensat aus und destilliert. Der Butyrolactongehalt des so gewonnenen y-Oxyl)utyraldehyds beträgt nur 0,2%.If all other things being equal are used at i gor one off Cobalt and copper on silica gel (20% Co, 1% Cu) existing at 17o ° in weak Hydrogen flow reduced catalyst, 33 to 35% of the 13ttanediol is transformed into y-oxy ~ butyraldelivd. The 13titvrolactc »i content of the product is o, 80/0. 13eisl) iel 2 About 75o cm3 of an atis cobalt copper spinel existing on silica gel Catalyst (16.2% Co, 8.8% Cu), which was reduced at 40o ° in a hydrogen stream, one passes hourly at 225 ° 6o cin3 pure i, 4-butanediol in a mixture with nitrogen. 40% of the 1,4-butanediol is converted into γ-oxyliutyraldehyde. plan drives out the y-oxybutyral (leliyd is removed from the reaction product with water vapor, and the condensate is etherified out and distilled. The butyrolactone content of the γ-oxyl) utyraldehyde obtained in this way is only 0.2%.
Arbeitet .man unter sonst gleichen Bedingungen mit einem Kobaltkupferspinell (64,8% Co, 352% Cu) ohne Träger, der zu Strängen von 4 X 6 mm verformt und bei 40o° im schwachen Wasserstoffstrom reduziert worden ist, bei 23o°, so werden ebenfalls 40% des Butandiols zu y-Oxybutyraldehyd umgesetzt. Der aufgearbeiteteAldehyd enthält nur 0,3% Butyrolacton.You work with a cobalt copper spinel under otherwise identical conditions (64.8% Co, 352% Cu) without carrier, which deforms into strands of 4 X 6 mm and at 40o ° has been reduced in the weak stream of hydrogen, at 23o °, so will also 40% of the butanediol converted to y-oxybutyraldehyde. The reprocessed aldehyde contains only 0.3% butyrolactone.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEB2126A DE832291C (en) | 1950-02-16 | 1950-02-17 | Process for the preparation of ª † -oxybutyraldehyde |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE1032333X | 1950-02-16 | ||
| DEB2126A DE832291C (en) | 1950-02-16 | 1950-02-17 | Process for the preparation of ª † -oxybutyraldehyde |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE832291C true DE832291C (en) | 1952-02-21 |
Family
ID=25964816
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DEB2126A Expired DE832291C (en) | 1950-02-16 | 1950-02-17 | Process for the preparation of ª † -oxybutyraldehyde |
Country Status (1)
| Country | Link |
|---|---|
| DE (1) | DE832291C (en) |
-
1950
- 1950-02-17 DE DEB2126A patent/DE832291C/en not_active Expired
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