CH239388A - Process for producing a drying oil from castor oil. - Google Patents
Process for producing a drying oil from castor oil.Info
- Publication number
- CH239388A CH239388A CH239388DA CH239388A CH 239388 A CH239388 A CH 239388A CH 239388D A CH239388D A CH 239388DA CH 239388 A CH239388 A CH 239388A
- Authority
- CH
- Switzerland
- Prior art keywords
- oil
- castor oil
- drying
- producing
- castor
- Prior art date
Links
- 239000003921 oil Substances 0.000 title claims description 11
- 239000004359 castor oil Substances 0.000 title claims description 8
- 235000019438 castor oil Nutrition 0.000 title claims description 8
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 title claims description 8
- 238000000034 method Methods 0.000 title claims description 7
- 238000001035 drying Methods 0.000 title claims description 6
- 239000003054 catalyst Substances 0.000 claims description 6
- 238000006243 chemical reaction Methods 0.000 claims description 6
- ILRRQNADMUWWFW-UHFFFAOYSA-K aluminium phosphate Chemical compound O1[Al]2OP1(=O)O2 ILRRQNADMUWWFW-UHFFFAOYSA-K 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 2
- 235000019198 oils Nutrition 0.000 description 7
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000001934 delay Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000000944 linseed oil Substances 0.000 description 1
- 235000021388 linseed oil Nutrition 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- WBHHMMIMDMUBKC-XLNAKTSKSA-N ricinelaidic acid Chemical group CCCCCC[C@@H](O)C\C=C\CCCCCCCC(O)=O WBHHMMIMDMUBKC-XLNAKTSKSA-N 0.000 description 1
- 150000003333 secondary alcohols Chemical class 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09F—NATURAL RESINS; FRENCH POLISH; DRYING-OILS; OIL DRYING AGENTS, i.e. SICCATIVES; TURPENTINE
- C09F5/00—Obtaining drying-oils
- C09F5/06—Obtaining drying-oils by dehydration of hydroxylated fatty acids or oils
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Catalysts (AREA)
Description
Verfahren zur Herstellung eines trocknenden Öls aus Rizinusöl. Die Anmeldung bezieht sich auf ein Ver fahren zur Herstellung eines trocknenden Öls aus Rizinusöl durch Wasserabspaltung.
Bisher wurde angenommen (vergleiche niederl. Patentschrift Nr. 25489), dass. Rizi- nusöl infolge seiner nicht trocknenden Eigen schaften für anstrichtechnische Zwecke un geeignet ist, und man hat versucht, durch be stimmte chemische Umwandlungen dieser Schwierigkeit entgegenzutreten.
Das Verfahren ist dadurch gekennzeich net, dass das Rizinusöl im Vakuum mit einer solchen Gewichtsmenge Aluminiumphosphat als Katalysator, die wenige Prozente der Ge wichtsmenge des zu verarbeitenden Öls be trägt, auf eine Temperatur von zirka 280 C erhitzt wird. Es ist an sich nicht neu, für einen ähnlichen Zweck bestimmte Katalysa toren zu verwenden; es hat sich aber heraus gestellt, dass ein überraschender Erfolg er zielt wird, wenn man als Katalysator Alumi- niumphosphat benutzt.
Die -Reaktion ist mit der Wasserabspaltung aus einem sekundären Alkohol vergleichbar, wodurch eine zweite Doppelbindung in dem Rizinolsäurerest ent steht, konjugiert mit der bereits bestehenden Doppelbindung.
Es hat sich dabei herausgestellt, da.B die Hinzufügung weniger Prozente Aluminium- phosphat die Dehydratierung fördert und die Eindickung des bereits gebildeten trocknen den Öls verzögert und, im Gegensatz zu allen bisher angewendeten Verfahren, der Erfolg erzielt wird, dass die Farbe des Öls sehr hell bleibt und Unreinheiten absorbiert werden.
Durch das Arbeiten im Vakuum ver meidet man zu gleicher Zeit die Einwirkung der Luft, und man kann die flüchtigen Stoffe, welche bei der Reaktion entstehen, leicht eliminieren.
<I>Beispiel:</I> In einem doppelwandigen Vakuumkessel, versehen mit einer Rührvorrichtung und einer Ableitung zum Kondensator und zur Vakuumpumpe, wird Rizinusöl langsam unter einem Vakuum von etwa 15 mm Queck- silberdruck während ungefähr 5 Stunden mit 5 % ALPO" bezogen auf das Gewicht des Ri zinusöls, bis auf zirka 280 C erhitzt.
Der Katalysator wird zweckmässih vorher frisch präzipitiert. gewaschen und vorsichtig getrocknet.
Es ist vorteilhaft. vor der Beendigung der Reaktion Dampf durch das (>1 hin durchzuleiten, um die noch vorhandenen flüchtigen Stoffe abzudestillieren. Nach Ab lauf der Reaktion filtriert man den Kataly sator ab.
Das erzielte Ö1 ist Hellfarbig und trock net, sikkativiert, ebenso schnell wie Leinöl.
Process for producing a drying oil from castor oil. The application relates to a process for the production of a drying oil from castor oil by dehydration.
So far it has been assumed (see Dutch patent specification No. 25489) that castor oil is unsuitable for painting purposes due to its non-drying properties, and attempts have been made to counteract this difficulty by means of certain chemical conversions.
The process is characterized in that the castor oil is heated to a temperature of approx. 280 C in a vacuum with an amount by weight of aluminum phosphate as a catalyst that is a few percent of the amount by weight of the oil to be processed. It is not in itself new to use certain catalysts for a similar purpose; However, it has been found that a surprising success is achieved if aluminum phosphate is used as the catalyst.
The reaction is comparable to the elimination of water from a secondary alcohol, which creates a second double bond in the ricinoleic acid residue, conjugated with the existing double bond.
It has been found that the addition of a small percentage of aluminum phosphate promotes dehydration and delays the thickening of the already formed drying oil and, in contrast to all previously used methods, the result is that the color of the oil is very much remains bright and impurities are absorbed.
By working in a vacuum, you avoid exposure to air at the same time and you can easily eliminate the volatile substances that arise during the reaction.
<I> Example: </I> In a double-walled vacuum kettle equipped with a stirrer and a discharge line to the condenser and the vacuum pump, castor oil is slowly drawn under a vacuum of about 15 mm mercury pressure for about 5 hours with 5% ALPO " to the weight of the Ri zine oil, heated to around 280 C.
The catalyst is expediently freshly precipitated beforehand. washed and carefully dried.
It's beneficial. Before the end of the reaction, pass steam through the (> 1 in order to distill off the volatile substances still present. After the reaction has ended, the catalyst is filtered off.
The oil obtained is light colored and dry, siccativates, just as fast as linseed oil.
Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CH239388T | 1944-01-11 |
Publications (1)
Publication Number | Publication Date |
---|---|
CH239388A true CH239388A (en) | 1945-10-15 |
Family
ID=4461180
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CH239388D CH239388A (en) | 1944-01-11 | 1944-01-11 | Process for producing a drying oil from castor oil. |
Country Status (1)
Country | Link |
---|---|
CH (1) | CH239388A (en) |
-
1944
- 1944-01-11 CH CH239388D patent/CH239388A/en unknown
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