US1882002A - Process for refining mineral oil - Google Patents
Process for refining mineral oil Download PDFInfo
- Publication number
- US1882002A US1882002A US474061A US47406130A US1882002A US 1882002 A US1882002 A US 1882002A US 474061 A US474061 A US 474061A US 47406130 A US47406130 A US 47406130A US 1882002 A US1882002 A US 1882002A
- Authority
- US
- United States
- Prior art keywords
- oil
- triethanolamine
- mineral oil
- refining mineral
- volume
- 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 - Lifetime
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M175/00—Working-up used lubricants to recover useful products ; Cleaning
- C10M175/0016—Working-up used lubricants to recover useful products ; Cleaning with the use of chemical agents
Definitions
- My invention relates to the refinement of mineral oils and is especially applicable to mineral oils containing suspended and dissolved impurities which have been produced by oxidation or cracking of the oils.
- the processes which have hitherto been in general use for refining these oils involve treatment of the oils with solutions of inorganic alkaline materials or with sulfuric acid.
- the disadvantages in these processes are the tendency to formation of very stable emulsions and the difliculty of complete removal of the treating agent, whose presence in the refined oil is objectionable.
- the amount of triethanolamine which should be added will, of course, vary with the degree of contamination of the oil by oxidized and cracked products. Aslittle as 5 by volume of commercial triethanolamine 1s sometimes suflicient, while as high as 1 may be added, although so large a percentage is seldom, if ever, required.
- the treating agent is a product which contains triethanolamine, the minimum amount of the treating agent must be increased so that not less than about by volume of triethanolamine will be present in the mixture.
- the temperature at which the process is conducted may vary considerably from that specified. The process does not exclude treatment of the oil, usually prior to the final bleaching, for removal of any undesirable high boiling constituents.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Lubricants (AREA)
Description
Patented Oct. 11, 1932 UNITED STATES PATENT orricu MELVIN A. DIETRICH, F POUGHKEEYSIE, NEW YORK, ASSIGNOR TO THE DE LAVAL SEPABATOR COMPANY, OF NEW YORK, N. Y A CORPORATION OF NEW JERSEY PROCESS ron ammme mum on.
No Drawing.
My invention relates to the refinement of mineral oils and is especially applicable to mineral oils containing suspended and dissolved impurities which have been produced by oxidation or cracking of the oils. The processes which have hitherto been in general use for refining these oils involve treatment of the oils with solutions of inorganic alkaline materials or with sulfuric acid. The disadvantages in these processes are the tendency to formation of very stable emulsions and the difliculty of complete removal of the treating agent, whose presence in the refined oil is objectionable.
I have found that these difiiculties are avoided by treating the oil with triethanolamine, either with or without prior or subsequent addition of water. By this method the suspended and dissolved impurities are coag- 2 ulated or thrown out of solution and can readily be removed by any suitable means. An appreciable-reduction in the quantity of material of an acidic nature in the oil is effected.
By the term triethanolamine I wish to include pure triethanolamine and those products known as commercial triethanolamine or also those products containing a substantial proportion of triethanolamine.
In some cases, especially in the treatment of a dark-colored oil, it may be advisable to further treat the oil in known manner with a bleaching agent whereby the color of the oil is considerabl improved.
The following specific example illustrates a preferred way of carrying out my improv rocess. A mineral oil which has been used 111 an internal combustion engine and contained 4.5% by volume of finely divided suspended carbon and which had a neutralization value of 0.51 mg. potassium hydroxide per gram of oil was heated to 90 C. and
by volume of triethanolamine was added, fol lowed by 25% by volume of hot water. The mixture was agitated at 90 C. for one-half hour and then separated by passa e through a centrifugal purifier. The puri ed oilwas clean and bright, contained no sediment, and
had a neutralization number of 0.25 m
potassium hydroxide per gram of oil. T e
oil was then given a treatment with 15% by Application filed August 8, 1980. Serial No. 474,061.
The amount of triethanolamine which should be added will, of course, vary with the degree of contamination of the oil by oxidized and cracked products. Aslittle as 5 by volume of commercial triethanolamine 1s sometimes suflicient, while as high as 1 may be added, although so large a percentage is seldom, if ever, required. When the treating agent is a product which contains triethanolamine, the minimum amount of the treating agent must be increased so that not less than about by volume of triethanolamine will be present in the mixture. The temperature at which the process is conducted may vary considerably from that specified. The process does not exclude treatment of the oil, usually prior to the final bleaching, for removal of any undesirable high boiling constituents.
What I claim and desire to protect by Letters Patent is:
1. The process of treating used mineral lubricating oil containing suspended and dissolved impurities produced by oxidation and cracking in order to effect the removal of such impurities which comprises adding to the oil not less than one-tenth of one percent of triethanolamine to effect coagulation of said impurities and separating the reaction products from the oil. I
2. The process of treating used mineral lubricating oil containing suspended and disd solved impurities produced by oxidation and cracking in order to effect the removal of such impuritles which comprises adding to the oil not less than one-tenth of one percent of triethanolamine and also hot water, and separating the reaction products from the oil.
In testimony of which invention, I have hereunto set my hand, at Poughkeepsie, New
York, on this fourth day of August, 1930.
MELVIN A. DIETRICH.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US474061A US1882002A (en) | 1930-08-08 | 1930-08-08 | Process for refining mineral oil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US474061A US1882002A (en) | 1930-08-08 | 1930-08-08 | Process for refining mineral oil |
Publications (1)
Publication Number | Publication Date |
---|---|
US1882002A true US1882002A (en) | 1932-10-11 |
Family
ID=23882028
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US474061A Expired - Lifetime US1882002A (en) | 1930-08-08 | 1930-08-08 | Process for refining mineral oil |
Country Status (1)
Country | Link |
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US (1) | US1882002A (en) |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2435734A (en) * | 1941-05-31 | 1948-02-10 | Ulric B Bray | Method of and apparatus for filtering oil |
US2568583A (en) * | 1949-06-18 | 1951-09-18 | Dow Chemical Co | Method of separating impurities from used lubricating oils |
US2951031A (en) * | 1958-05-07 | 1960-08-30 | Stanton D Barclay | Process for purifying oil with monoisopropanolamine |
US3003350A (en) * | 1960-12-08 | 1961-10-10 | Ralph L Faber | Method of examining oil samples |
US3112258A (en) * | 1958-11-12 | 1963-11-26 | Standard Oil Co | Process for the recovery of minor amounts of solvent from solventextracted hydrocarbons |
FR2005199A1 (en) * | 1969-04-25 | 1969-12-12 | Picot Jean | Regeneration of used oils |
US3617530A (en) * | 1969-11-12 | 1971-11-02 | Atlantic Richfield Co | Metals removal from heavy hydrocarbon fractions |
US4028226A (en) * | 1975-11-12 | 1977-06-07 | The Lubrizol Corporation | Method of rerefining oil with recovery of useful organic additives |
US4105538A (en) * | 1977-01-21 | 1978-08-08 | Mattox William J | Process for the refining of used motor oils and products thereof |
US4370238A (en) * | 1979-05-14 | 1983-01-25 | Marathon Oil Company | Process for drying surfactant-containing crude oil |
US4789460A (en) * | 1987-08-10 | 1988-12-06 | Phillips Petroleum Company | Process for facilitating filtration of used lubricating oil |
GB2567884A (en) * | 2017-10-31 | 2019-05-01 | Ffs Refiners Pty Ltd | Method for the recycling used lubricating oils |
-
1930
- 1930-08-08 US US474061A patent/US1882002A/en not_active Expired - Lifetime
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2435734A (en) * | 1941-05-31 | 1948-02-10 | Ulric B Bray | Method of and apparatus for filtering oil |
US2568583A (en) * | 1949-06-18 | 1951-09-18 | Dow Chemical Co | Method of separating impurities from used lubricating oils |
US2951031A (en) * | 1958-05-07 | 1960-08-30 | Stanton D Barclay | Process for purifying oil with monoisopropanolamine |
US3112258A (en) * | 1958-11-12 | 1963-11-26 | Standard Oil Co | Process for the recovery of minor amounts of solvent from solventextracted hydrocarbons |
US3003350A (en) * | 1960-12-08 | 1961-10-10 | Ralph L Faber | Method of examining oil samples |
FR2005199A1 (en) * | 1969-04-25 | 1969-12-12 | Picot Jean | Regeneration of used oils |
US3617530A (en) * | 1969-11-12 | 1971-11-02 | Atlantic Richfield Co | Metals removal from heavy hydrocarbon fractions |
US4028226A (en) * | 1975-11-12 | 1977-06-07 | The Lubrizol Corporation | Method of rerefining oil with recovery of useful organic additives |
US4105538A (en) * | 1977-01-21 | 1978-08-08 | Mattox William J | Process for the refining of used motor oils and products thereof |
US4370238A (en) * | 1979-05-14 | 1983-01-25 | Marathon Oil Company | Process for drying surfactant-containing crude oil |
US4789460A (en) * | 1987-08-10 | 1988-12-06 | Phillips Petroleum Company | Process for facilitating filtration of used lubricating oil |
GB2567884A (en) * | 2017-10-31 | 2019-05-01 | Ffs Refiners Pty Ltd | Method for the recycling used lubricating oils |
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