CH315585A - Process for the production of alcohols from lower molecular weight alcohols - Google Patents
Process for the production of alcohols from lower molecular weight alcoholsInfo
- Publication number
- CH315585A CH315585A CH315585DA CH315585A CH 315585 A CH315585 A CH 315585A CH 315585D A CH315585D A CH 315585DA CH 315585 A CH315585 A CH 315585A
- Authority
- CH
- Switzerland
- Prior art keywords
- alcohols
- carbon oxide
- water vapor
- catalysts
- partial pressure
- Prior art date
Links
- 150000001298 alcohols Chemical class 0.000 title claims description 15
- 238000000034 method Methods 0.000 title claims description 8
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 18
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 15
- 229910002090 carbon oxide Inorganic materials 0.000 claims description 15
- 235000019441 ethanol Nutrition 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 239000003054 catalyst Substances 0.000 claims description 10
- 238000006243 chemical reaction Methods 0.000 claims description 10
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 6
- 230000015572 biosynthetic process Effects 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- 238000003786 synthesis reaction Methods 0.000 claims description 6
- 229910052751 metal Inorganic materials 0.000 claims description 5
- 239000002184 metal Substances 0.000 claims description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 4
- 229910017052 cobalt Inorganic materials 0.000 claims description 4
- 239000010941 cobalt Substances 0.000 claims description 4
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 4
- 239000007789 gas Substances 0.000 claims description 4
- 229910052739 hydrogen Inorganic materials 0.000 claims description 4
- 239000001257 hydrogen Substances 0.000 claims description 4
- 150000001875 compounds Chemical class 0.000 claims description 3
- 230000000737 periodic effect Effects 0.000 claims description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 2
- 239000005909 Kieselgur Substances 0.000 claims description 2
- 241000895215 Metallea Species 0.000 claims description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 2
- 229910004369 ThO2 Inorganic materials 0.000 claims description 2
- KXKVLQRXCPHEJC-UHFFFAOYSA-N acetic acid trimethyl ester Natural products COC(C)=O KXKVLQRXCPHEJC-UHFFFAOYSA-N 0.000 claims description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 2
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 claims description 2
- -1 carbonyl hydrogen Chemical compound 0.000 claims description 2
- 239000003426 co-catalyst Substances 0.000 claims description 2
- 229910052802 copper Inorganic materials 0.000 claims description 2
- 239000010949 copper Substances 0.000 claims description 2
- 230000007423 decrease Effects 0.000 claims description 2
- 239000003792 electrolyte Substances 0.000 claims description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 2
- 150000004767 nitrides Chemical class 0.000 claims description 2
- 235000020075 ouzo Nutrition 0.000 claims description 2
- 238000002360 preparation method Methods 0.000 claims description 2
- ZCUFMDLYAMJYST-UHFFFAOYSA-N thorium dioxide Chemical compound O=[Th]=O ZCUFMDLYAMJYST-UHFFFAOYSA-N 0.000 claims description 2
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/32—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring increasing the number of carbon atoms by reactions without formation of -OH groups
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12C—BEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
- C12C11/00—Fermentation processes for beer
- C12C11/02—Pitching yeast
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Mycology (AREA)
- Microbiology (AREA)
- Food Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Biochemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Verfahren zur Herstellung von Alkoholen aus niedriger molekularen Alkoholen
Die vorliegende Erfindung betrifft ein Verfahren zur Herstellung von Alkoholen durch Umsetzung von Kohlenoxyd mit Wasserdampf und niedriger molekularen Alkoholen bei llöheren Temperaturen und gegebenenfalls erhöhten Drucken. Die Umsetzung von Alkoholen mit Kohlenoxyd und Wasserdampf ist bereits von K. Ziegler ¸PrÏparative organische Chemie , Band 36, Teil I, Dietriehsehe Verlagsbuchhandlung, 1948, Seiten 115-154, beschrieben worden. Diese Umsetzungen wur- den bisher in Gegenwart von Metallea. rbonylen und Metallearbonylwasserstoff als Kataly- satoren durchgef hrt.
Es wurde nun gefunden, da. die ge- nannte Umsetzung besonders vorteilhaft dureh- geführt werden kann, wenn man Katalysatoren verwendet, die mindestens ein Metall der 8. (truppe des periodisehen. Systems entweder als solches oder in Form einer Verbindung mit metallischem Bindungszustand, beispiels- weise als Carbid oder Nitrid, enthalten, und die Menge des angewandten Wasserdampfes so begrenzt, dass der Wasserdampfpartialdruck den Partialdruck des Kohlenoxyds nicht über sehreitet. Wird z.
B. der Wasserda. mpfpartialdruck des Synthesegasgemisehes so stark ver grössert, dass der Quotient Kohlenoxyd : Was serdampf den Wert 1 untersehreitet, so fällt die Menge des umgesetzten Kohlenoxyds infolge Konta. ktoxydation ständig ab, um im Verla. ufe kurzer Reaktionszeiten pra. ktiseh auf Null abzusinken, wobei die Katalysatoren innerhalb weniger Stunden unwirksam werden.
Die Umsetzung kann bei gewöhnlichem oder erhöhtem. Druek erfolgen.
Beispiel
Ein bei der Oxosynthese bekannter Co-Kata- lysator, bestehend aus Kobalt, ThO2, Kupfer und Kieselgur im Verhältnis 100 : 18 : 3 : 100 wird zunächst bei 400 und mit einer Raumge- schwindigkeit von 500 4 Stunden mit Elektrolytwasserstoff reduziert.
Nun setzt man einem Kohlenoxyd - Wasserdampf - Gemisch, welches auf 3 Mol Kohlenoxyd 1 Mol Wasser- dampf enthÏlt, 1 Mol Methanoldampf zu und leitet dieses Gas-Dampfgemisch unter einem Druck von 100 atü und bei einer Temperatur von 210 über den Kobaltkatalysator. Bei der Reaktion wird das Methanol zu etwa 30 /o verbraucht. Bei einem CO-Umsatz von 90 ouzo erscheint das verbrauchte Methanol im Syn- theseprodukt im wesentlichen als Äthylalkohol neben geringen Mengen Methyl-und Äthyl- acetat.
PATENTANSPR. UCH
Verfahren zur Herstellung von Alkoholen durci Umsetzen von Kohlenoxyd mit Wasser-
**WARNUNG** Ende DESC Feld konnte Anfang CLMS uberlappen**.
Process for the production of alcohols from lower molecular weight alcohols
The present invention relates to a process for the preparation of alcohols by reacting carbon monoxide with water vapor and lower molecular weight alcohols at lower temperatures and optionally elevated pressures. The reaction of alcohols with carbon oxide and steam has already been described by K. Ziegler ¸Pparative Organic Chemistry, Volume 36, Part I, Dietriehsehe Verlagsbuchhandlung, 1948, pages 115-154. These reactions were previously carried out in the presence of Metallea. Carbonyls and metal carbonyl hydrogen were used as catalysts.
It has now been found there. The aforementioned reaction can be carried out particularly advantageously if catalysts are used which contain at least one metal from the 8th group of the periodic system either as such or in the form of a compound with a metallic bond state, for example as a carbide or nitride , and the amount of water vapor used is limited in such a way that the water vapor partial pressure does not exceed the partial pressure of the carbon oxide.
B. the Wasserda. The partial pressure of the synthesis gas mixture increases so much that the quotient of carbon oxide: water vapor falls below the value 1, the amount of converted carbon oxide falls as a result of contact. ctoxydation constantly decreases in order to uf short response times pra. ktiseh drop to zero, the catalysts becoming ineffective within a few hours.
The implementation can be at ordinary or elevated. Druek done.
example
A co-catalyst known from oxo synthesis, consisting of cobalt, ThO2, copper and diatomaceous earth in a ratio of 100: 18: 3: 100, is first reduced with electrolyte hydrogen at 400 and at a space velocity of 500 for 4 hours.
Now, 1 mol of methanol vapor is added to a carbon oxide / steam mixture which contains 1 mol of steam for every 3 mol of carbon oxide, and this gas / steam mixture is passed over the cobalt catalyst at a pressure of 100 atmospheres and a temperature of 210. About 30% of the methanol is consumed in the reaction. With a CO conversion of 90 ouzo, the methanol consumed appears in the synthesis product essentially as ethyl alcohol in addition to small amounts of methyl and ethyl acetate.
PATENT CLAIM. UCH
Process for the production of alcohols by reacting carbon oxide with water
** WARNING ** End of DESC field could overlap beginning of CLMS **.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE315585X | 1951-08-01 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CH315585A true CH315585A (en) | 1956-08-31 |
Family
ID=6150230
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CH315585D CH315585A (en) | 1951-08-01 | 1952-07-10 | Process for the production of alcohols from lower molecular weight alcohols |
Country Status (1)
| Country | Link |
|---|---|
| CH (1) | CH315585A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2408567A1 (en) * | 1977-11-10 | 1979-06-08 | Chem Systems | PROCESS FOR PREPARING BETA-PHENYLETHYL ALCOHOL |
-
1952
- 1952-07-10 CH CH315585D patent/CH315585A/en unknown
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2408567A1 (en) * | 1977-11-10 | 1979-06-08 | Chem Systems | PROCESS FOR PREPARING BETA-PHENYLETHYL ALCOHOL |
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