DE942519C - Process for improving the odor of waste oil refined products - Google Patents
Process for improving the odor of waste oil refined productsInfo
- Publication number
- DE942519C DE942519C DEB28592A DEB0028592A DE942519C DE 942519 C DE942519 C DE 942519C DE B28592 A DEB28592 A DE B28592A DE B0028592 A DEB0028592 A DE B0028592A DE 942519 C DE942519 C DE 942519C
- Authority
- DE
- Germany
- Prior art keywords
- alcohol
- odor
- improving
- caustic
- waste oil
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G19/00—Refining hydrocarbon oils in the absence of hydrogen, by alkaline treatment
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Fats And Perfumes (AREA)
Description
Verfahren zur Geruchsverbesserung von Altölraffinaten Die bei der Regenerierung von Altölen anfallenden Raffinate haben trotz intensiver Raffination mit Säure, Alkali und Bleicherden nach Beseitigung der niedrigsiedenden Ölanteile durch Destillation einen unangenehmen Geruch, wodurch sich die Regenerate deutlich von Neuölraffmaten unterscheiden.Process for improving the odor of waste oil refinates Regeneration of waste oils have accumulated raffinates despite intensive refining with acid, alkali and fuller's earth after removal of the low-boiling oil components distillation gives off an unpleasant odor, which clearly shows the regenerated material differ from Neuölraffmaten.
Die unangenehmen Geruchsträger dürften auf Zusatzstoffe von Kraftstoffen, Ölzusätzen sowie auf den Schwefelgehalt der Dieselkraftstoffe zurückzuführen sein, die bei der Destillation bei Temperaturen von =50° und darüber zersetzt und durch das Bleichen mit Bleicherden besonders stark aktiviert werden.The unpleasant odor carriers are likely to be due to additives in fuels, Oil additives as well as the sulfur content of diesel fuels, which decomposes and penetrates during the distillation at temperatures of = 50 ° and above bleaching can be particularly strongly activated with fuller's earth.
Wie nun gefunden wurde, lassen sich die unangenehmen Geruchsträger durch ein sich an die Raffination anschließendes Auswaschen oder Auskochen mit einem alkoholischen Ätzalkali, Erdalkalihydrat oder mit Alkohol enthaltendem Ammoniak völlig entfernen. Zur Ausführung des Verfahrens kann z. B. mit Methyh oder Äthylalkohol versetzte Ätznatron-oder Ätzkalilauge Verwendung finden, ferner in Alkohol aufgeschwemmtes Calciumhydrat oder mit Alkohol vermischter Ammoniak.- Das hiermit behandelte Regenerat unterscheidet sich geruchlich nicht mehr von Neuölraffinaten. Gleichzeitig werden die Neutralisationszahlen und die Verseifungszahl günstig beeinlußt.As has now been found, the unpleasant odor carriers by washing or boiling with a after refining alcoholic caustic alkali, alkaline earth metal hydrate or ammonia containing alcohol remove completely. To carry out the method, for. B. with methyl or ethyl alcohol offset caustic soda or caustic potash are used, furthermore in alcohol Floated calcium hydrate or ammonia mixed with alcohol treated regrind no longer differs in smell from new oil refined. At the same time, the neutralization numbers and the saponification number are favorably influenced.
Das Auswaschen kann auf Waschkolonnen im Gegenstromprinzip, das Auskochen in heizbaren, geschlossenen, mit Rückflußkühlung und mit Rührwerken versehenen Kesseln erfolgen. Aus den behandelten Ölen wird der anhaftende Alkohol verdampft; dann wird mit Wasser ausgewaschen und getrocknet.The washing can be done on washing columns using the countercurrent principle, the boiling in heatable, closed boilers equipped with reflux cooling and stirrers take place. The adhering alcohol is evaporated from the treated oils; Then it will be washed out with water and dried.
Beispiel 3ooo kg Regenerat werden mit 5oo kg einer Lauge, die aus 25o kg Methyl- oder Äthylalkohol und 25o kg einer Ätznatronlauge von 3o° B6 besteht, im Rückfuß 1/2 Stunde gekocht und dann der Ruhe überlassen. Die sich absetzende alkoholische Lauge wird abgezogen; sie kann bis zur Erschöpfung, des Alkaligehaltes wieder Verwendung finden. Aus dem. abgesetzten Öl wird der anhaftende Alkohol durch Erhitzen entfernt. Das Öl wird mit heißem Wasser nachgewaschen und getrocknet.Example 300 kg of regenerate are mixed with 500 kg of a lye made from Consists of 25o kg of methyl or ethyl alcohol and 25o kg of caustic soda solution of 30 ° B6, Boiled in the hindfoot for 1/2 hour and then left to rest. The settling alcoholic lye is withdrawn; it can go up to exhaustion, the alkali content find use again. From the. The settled oil is carried through by the adhering alcohol Heating removed. The oil is washed with hot water and dried.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEB28592A DE942519C (en) | 1953-11-28 | 1953-11-28 | Process for improving the odor of waste oil refined products |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEB28592A DE942519C (en) | 1953-11-28 | 1953-11-28 | Process for improving the odor of waste oil refined products |
Publications (1)
Publication Number | Publication Date |
---|---|
DE942519C true DE942519C (en) | 1956-05-03 |
Family
ID=6962702
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEB28592A Expired DE942519C (en) | 1953-11-28 | 1953-11-28 | Process for improving the odor of waste oil refined products |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE942519C (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1672304A (en) * | 1924-08-18 | 1928-06-05 | Standard Oil Co California | Process of purifying mineral oils |
-
1953
- 1953-11-28 DE DEB28592A patent/DE942519C/en not_active Expired
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1672304A (en) * | 1924-08-18 | 1928-06-05 | Standard Oil Co California | Process of purifying mineral oils |
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