US1761328A - Process of purifying lubricating-oil distillates - Google Patents
Process of purifying lubricating-oil distillates Download PDFInfo
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- US1761328A US1761328A US296629A US29662928A US1761328A US 1761328 A US1761328 A US 1761328A US 296629 A US296629 A US 296629A US 29662928 A US29662928 A US 29662928A US 1761328 A US1761328 A US 1761328A
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- Prior art keywords
- acid
- lubricating oil
- oil
- treated
- water solution
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- 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
Links
- 239000010687 lubricating oil Substances 0.000 title description 39
- 238000000034 method Methods 0.000 title description 18
- 239000002253 acid Substances 0.000 description 46
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 41
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 39
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 36
- 239000003921 oil Substances 0.000 description 28
- 239000000470 constituent Substances 0.000 description 26
- 229910052500 inorganic mineral Inorganic materials 0.000 description 20
- 235000010755 mineral Nutrition 0.000 description 20
- 239000011707 mineral Substances 0.000 description 20
- 150000007524 organic acids Chemical class 0.000 description 19
- 150000007513 acids Chemical class 0.000 description 17
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 15
- 230000001804 emulsifying effect Effects 0.000 description 15
- 239000001117 sulphuric acid Substances 0.000 description 14
- 235000011149 sulphuric acid Nutrition 0.000 description 14
- 238000006386 neutralization reaction Methods 0.000 description 13
- 235000011121 sodium hydroxide Nutrition 0.000 description 13
- 230000003472 neutralizing effect Effects 0.000 description 10
- 239000010802 sludge Substances 0.000 description 8
- 239000000839 emulsion Substances 0.000 description 6
- 235000005985 organic acids Nutrition 0.000 description 6
- 150000003839 salts Chemical class 0.000 description 6
- 239000010688 mineral lubricating oil Substances 0.000 description 5
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 4
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000003208 petroleum Substances 0.000 description 4
- -1 sulpho organic acid Chemical class 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 239000010426 asphalt Substances 0.000 description 2
- 230000001050 lubricating effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000002085 persistent effect Effects 0.000 description 2
- 239000013535 sea water Substances 0.000 description 2
- 235000010269 sulphur dioxide Nutrition 0.000 description 2
- 239000004291 sulphur dioxide Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004042 decolorization Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- STZCRXQWRGQSJD-GEEYTBSJSA-M methyl orange Chemical compound [Na+].C1=CC(N(C)C)=CC=C1\N=N\C1=CC=C(S([O-])(=O)=O)C=C1 STZCRXQWRGQSJD-GEEYTBSJSA-M 0.000 description 1
- 229940012189 methyl orange Drugs 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 159000000001 potassium salts Chemical class 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
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
- C10G17/00—Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge
- C10G17/02—Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge with acids or acid-containing liquids, e.g. acid sludge
- C10G17/04—Liquid-liquid treatment forming two immiscible phases
- C10G17/06—Liquid-liquid treatment forming two immiscible phases using acids derived from sulfur or acid sludge thereof
Definitions
- This invention relates to a process of purifying viscous mineral oil fractions for the production of lubricating oils, to extract therefrom constituents which operate to produce emulsions when commingled with water, or a water solution of caustic soda, and which alfo operate to hinder decolorization of the o1
- An object of the invention is to purif mineral lubricating oil distillates to pro uce a treated oil which will not form persistent emulsions with water, a water solution of caustic soda or water containing dissolved mineral salts, such as sea water.
- Another object of the invention is to pro- Vide a process of treating viscous petroleum oil distillates without the formation of persistent emulsions during treatment thereof and without any substantial loss of the finished lubricating oil.
- Another object of the invention is to pro-
- the lubricant may come into contact or become commingled with water or steam.
- Another object of the invention is to produce a lubricating oil free from emulsifying constituents such as resins, gums, organic.
- emulsifying agents such as organic acids, oxy and oxy-sulpho-acids, which have a preferential oil solubility and remain in solution in the treated lubricating oil stock after the acid sludge has been separated from the oil.
- organic acids, oxy and oxy-sulpho-acids which have a preferential oil solubility and remain in solution in the treated lubricating oil stock after the acid sludge has been separated from the oil.
- the neutralization operation in two steps, the first step comprising adding and commingling with the acid treated lubricating oil, a water solution of caustic soda in quantitiesjust sufficient to substantially neutralize all the sulphuric and sulphurous acid present, and without any substantial.neutralization of the organic or sulpho-organic acid constituents present, whereby oil and water emulsions are not formed.
- the quantity of the water solution of caustic soda required to neutralize the sulphuric and sulphurous acids present is determined by titrating a sample of the acidtratedlubricating oil stock with the water solution of caustic soda to be employed, using any of the well known indicators which are not sensitive to organic acids, such as methyl orange.
- the lubricating oil stock is separated from the water containing the products of neutralization and is then completely neutralized by commingling with a water solution of potassium hydroxide and steam at a pressure ofapproximately 50 pounds gauge.
- the introduction of steam is continued until a temperature of approximately 250 to 280 degrees F. is attained, after which the introduction of steam is discontinued and the water solution of salts and excess potassium hydroxide separated therefrom.
- a lubricating oil distillate of 18 to 21 degrees B. derived b vacuum distillation of an asphalt or mixed ase crude petroleum oil may first be treated with 4 pound of 66 degree B. sulphuric acid per gallon of oil and subsequently with successive ap lications of from A to as hi h as 2 pounds or igher of sulphuric acid havmg a strength ranging from 93 per cent sulphuric acid to as high as 15 per cent fuming sulphuric acid per gallon of oil, this treatment depending upon the stock treated and the product desired, the acid being agitated with the oil and the sludge formed being removed prior to the application of each succeeding portion of acid used.
- the acid treated oil in this second agitator is then commingled with a water solution of caustic soda added in quantities just suflicient to neutralize the free sulphur dioxide or sulphurous acid and free sulphuric acid present, and without any substantial neutralization of the organic or sulpho organic acid constituents present, with the application of heat at a temperature of approximately to degrees F., after which the water containing the products of neutraliza-' tion free from oil emulsions, is separated from the partly neutralized treated oil by withdrawing the same from the bottom of the agitator or treating tank after settling.
- the oil is commingled with a water solution of potassium hydroxide in quantities sulficientto complete 1y neutralize all the organic and sulpho acid constituents present, preferably in the same agitator and then transferring the same in a commingled state to a pressure treatingtank provided with means for introducing steam into the commingledmixture under pressure. Steam is then.
- the purified lubricating oil stock now free of emulsifyingconstituents is preferably again distilled under a vacuum in order to separate the various grades of lubricating oil stocks and thereafter clarified I and decolorized to the required degree by the employment of a decolorizing agent, or the treated lubricating oil stock may be clarified and decolorized to the required degree by methods known in the art, without a re-distillation operation, or may be employed directly without further treatment.
- free mineral acids mean uncombined sulphur dioxide, sulphurous, or sulphuric acid, which may be present in the lubricating oil stock after treatment with sulphuric acid.
- That step in the process of purifying mineral lubricating oil stocks after treatment with sulphuric acid and removal of the acid sludge therefrom comprising, first neutrallzing and separating the free mineral acids as water soluble mineral acid salts, from the acid treated lubricating oil stock, without any substantial neutralization of the organic acid, or sulpho-acids present, then neutralizing the organic acids and sul ho-acids-by commingling the acid treated oi from which the saidmineral acids have been removed, with awater solution of potassium hydroxide and finally separating the neutralized organic acids and sulpho organic acids from the treated oil by subjecting the treated oil commingled with the water solution of potassium hydroxide to a temperature of approximately 250 to 280 degrees F. at a pressure of approximately 50 pounds gauge, produced by the introduction of steam into the mixture.
- That step in the process of purifying mineral lubricating oil stocks after treatment with sulphuric acid and removal of the acid sludge therefrom comprising, first neutralizing the free mineral acids in the acid treated lubricating oil stock with a watersolutlon of caustic soda introduced in quantitles ust sufiicient to substantially neutralize all free 1 vmineral acids present, without any substantial neutralization of the organic acid emulsifying constituents present, separating and removing the water solution of mineral acid salts from the lubricating oil stock and then commingling the lubricating oil stock from which the free mineral acids have been removed, with a' water solution of potassium hydroxide in quantities sufficient to neutralize the organic acid emulsifying constituents present and thenseparating a water solution of the neutralized organic acid emulsifying constituents from the lubricating oil stock by subjecting the same to a temperature of approximately 250 to 280. degrees F. at a pressureof approximately 50 pounds gauge.
- That step in the process of purifying mineral lubricating oil stocks after treatment with sulphuric acid and removal of the acid sludge therefrom comprising, neutralizing the free mineral acids in an acid treated lubricating oil stock with a water solution of caustic soda introduced in quantities just sufficient to substantially neutralize all free mineral acids present and without any substantial neutralization of the organic acid emulsifying constituents contained therein, separating and removing the water solution of mineral acid salts from the lubricating oil stock and then commingling the lubricating oil stock from which the free mineral acids have been removed, with a water solution of potassium hydroxide in quantities sufficient to neutralize all the organic acid emulsifying constituents present, and then separating a water solution of the'neutralized organic acid en1ul- 'sifyin' constituents from the lubricating oil stock y subjecting the same to a temperature of approximately 250 to 280 degrees F. at a pressure of approximately 50 pounds produced by the introduction of steam into the commingled mixture. 7
- a process of urifying mineral lubrieating oil stocks a ter treatment with sulphuric acid ,,forti'1'e removal of emulsifying constituents comprising, neutralizing and removing the free mineral acids from an acid treated lubricating oil stockvfrom which the' acid sludge has been substantially removed, with a water solution of caustic soda, without any substantial neutralization or removal of the or anic acid constituents contained therein an then removing the organic acid const1tuents by commingling the said acidtreated lubricating oil stock from which the free mineral acids have been removed, with an ex-' cess of a water solution of potassium hydroxide at a temperature of approximately 250 to 280 F., and finally separating the neutralized organic acids from the lubricating oil stock.
- a process of purifying mineral lubricating.oil stocks after treatment with sulphuric acid,-for the removal of the emulsifyand removing the free mineral acids from an acid treated lubricating oil'stock from which the acid sludge has been substantially removed, with a water solution of caustic soda without any substantial neutralization of the organic acid constituents contained therein and then removing the organic acid constituents by commin ling the acid treated lubricating oil stock rom which the free mineral acids have been removed, with an excess of a water solution of potassium hydroxide and finally separating a water solution containing the neutralized organic acid constituents from the lubricating oil stock at a temperature of approximately 250 to 280 degrees F. and at a pressure of approximately 50 pounds.
- a process of urifying mineral lubricating oil stocks a er treatment with sulphuric acid and removal of the acid sludge therefrom comprising, neutralizing the free mineral acids in an acid treated lubricating oil stock, by commingling the same with the requisite quantity of a water solution of sodium hydroxide at a temperature of ap roximately 150 degrees F.
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- 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)
- Lubricants (AREA)
Description
Patented June 3, 1930 UNITED STATES PATENT OFFICE MARVIN L. CHAPIPELL, OF WATSON, CALIFORNIA, ASSIGNQR, IBY MESNE ASSIGNMENTS, TO RIGHFIELD OIL COMPANY OF CALIFORNIA, OF LOS ANGELES, CALIFORNIA, A
CORPORATION OF DELAWARE PROCESS OF PURIFYING LUBRICATING-OIL DISTILLATES No Drawing. Application filed July 31,
This invention relates to a process of purifying viscous mineral oil fractions for the production of lubricating oils, to extract therefrom constituents which operate to produce emulsions when commingled with water, or a water solution of caustic soda, and which alfo operate to hinder decolorization of the o1 An object of the invention is to purif mineral lubricating oil distillates to pro uce a treated oil which will not form persistent emulsions with water, a water solution of caustic soda or water containing dissolved mineral salts, such as sea water.
Another object of the invention is to pro- Vide a process of treating viscous petroleum oil distillates without the formation of persistent emulsions during treatment thereof and without any substantial loss of the finished lubricating oil.
Another object of the invention is to pro-,
duce a lubricating oil suitable for lubricating steam turbines or other machinery in which.
the lubricant may come into contact or become commingled with water or steam.
Another object of the invention is to produce a lubricating oil free from emulsifying constituents such as resins, gums, organic.
acids, phenols, or organic sulphd acids.
Other objects and advantages will appear in the practical use of the same from the following description.
During the treatment of lubricating oil stock's derived from an asphalt base crude petroleum oil, with sulphuric acid, certain emulsifying agents are formed, such as organic acids, oxy and oxy-sulpho-acids, which have a preferential oil solubility and remain in solution in the treated lubricating oil stock after the acid sludge has been separated from the oil. These emulsifying constituents cannot be completely'removed from the oil by any of the well-known methods of neutralizing with caustic soda and washing with water.
By these well-known methods of neutralizing an acid treated lubricating oil with caustic soda and washing with water, a certain percentage of the treated lubricating oil is emulsified with the water solution of cans- 1928. Serial No. 296,629.
tic soda and the removal thereof diminishes the yield of said treated oil. Also, a portion of the said emulsifying constituents remain in the treated oil, which causes the same to form emulsion when used to lubricate steam turbines in which the oil comes into contact w1th water or sea-water employed in the coolmg system. In particular, in the manufacture of lubricating oils from an as halt 'or mixed base crude petroleum oil, y well: known methods, there is lost during the neu-'' tralizing and washing operation from 5 to 15 per cent by volume of the treated oil, and
under the most'favorable .conditions only an veloped with s'ome success to employ alcohol and other like solvents to remove the emulsifying constituents which occur naturally or. those produced in the acid treatment of lubricating oil stocks.
I have discovered that superior results can be obtained by performing the neutralization operation in two steps, the first step comprising adding and commingling with the acid treated lubricating oil, a water solution of caustic soda in quantitiesjust sufficient to substantially neutralize all the sulphuric and sulphurous acid present, and without any substantial.neutralization of the organic or sulpho-organic acid constituents present, whereby oil and water emulsions are not formed. The quantity of the water solution of caustic soda required to neutralize the sulphuric and sulphurous acids present is determined by titrating a sample of the acidtratedlubricating oil stock with the water solution of caustic soda to be employed, using any of the well known indicators which are not sensitive to organic acids, such as methyl orange. After this first neutralizing step, the lubricating oil stock is separated from the water containing the products of neutralization and is then completely neutralized by commingling with a water solution of potassium hydroxide and steam at a pressure ofapproximately 50 pounds gauge. The introduction of steam is continued until a temperature of approximately 250 to 280 degrees F. is attained, after which the introduction of steam is discontinued and the water solution of salts and excess potassium hydroxide separated therefrom.
By this method a complete neutralization and separationof substantially all the emulsifying constituents is effected and the treated lubricating oil stock is thereafter decolorized to the required degree by methods known in the art.
The following describes the preferred method of carrying out this invention.
For illustration, a lubricating oil distillate of 18 to 21 degrees B. derived b vacuum distillation of an asphalt or mixed ase crude petroleum oil, may first be treated with 4 pound of 66 degree B. sulphuric acid per gallon of oil and subsequently with successive ap lications of from A to as hi h as 2 pounds or igher of sulphuric acid havmg a strength ranging from 93 per cent sulphuric acid to as high as 15 per cent fuming sulphuric acid per gallon of oil, this treatment depending upon the stock treated and the product desired, the acid being agitated with the oil and the sludge formed being removed prior to the application of each succeeding portion of acid used.
After the removal of substantially all of the acid slud e from the treated oil, it is in condition to e neutralized and freed from the emulsifying constituents, which iscarried out by preferably transferring the treated oil to a second agitator or treating tank provided with heating means such as a steam coil. The acid treated oil in this second agitator is then commingled with a water solution of caustic soda added in quantities just suflicient to neutralize the free sulphur dioxide or sulphurous acid and free sulphuric acid present, and without any substantial neutralization of the organic or sulpho organic acid constituents present, with the application of heat at a temperature of approximately to degrees F., after which the water containing the products of neutraliza-' tion free from oil emulsions, is separated from the partly neutralized treated oil by withdrawing the same from the bottom of the agitator or treating tank after settling.
After this first artial neutralizing step and separation of t e oil from the water and products of neutralization, the oil is commingled with a water solution of potassium hydroxide in quantities sulficientto complete 1y neutralize all the organic and sulpho acid constituents present, preferably in the same agitator and then transferring the same in a commingled state to a pressure treatingtank provided with means for introducing steam into the commingledmixture under pressure. Steam is then. introduced into the neutralized treated oil mixture until a temp erature of a proximately 250 to 280 degrees is obtaine at a pressure of approximately 50 pounds gauge, after which the steam is shut oflf' and the treated oil-permitted to separate from the water component which contains the emulsifying constituents in solution as water soluble potassium salts, together with the excess potassium hydroxide employed in the neutralization operation, which is separated from the oil by withdrawing from the bottom of the said pressure treating tank. The purified lubricating oil stock now free of emulsifyingconstituents, is preferably again distilled under a vacuum in order to separate the various grades of lubricating oil stocks and thereafter clarified I and decolorized to the required degree by the employment of a decolorizing agent, or the treated lubricating oil stock may be clarified and decolorized to the required degree by methods known in the art, without a re-distillation operation, or may be employed directly without further treatment.
By the term free mineral acids I mean uncombined sulphur dioxide, sulphurous, or sulphuric acid, which may be present in the lubricating oil stock after treatment with sulphuric acid.
While the process herein described is well adapted for carrying out the object of the invention, it is to be understood that various changes and modifications may be made without departing from the spirit of the in,- vention and the invention includes all such changes and modifications as come within the scope of the appended claims.
What I claim is:
1. That step in the process of purifying mineral lubricating oil stocks after treatment with sulphuric acid and removal of the acid sludge therefrom, comprising, first neutrallzing and separating the free mineral acids as water soluble mineral acid salts, from the acid treated lubricating oil stock, without any substantial neutralization of the organic acid, or sulpho-acids present, then neutralizing the organic acids and sul ho-acids-by commingling the acid treated oi from which the saidmineral acids have been removed, with awater solution of potassium hydroxide and finally separating the neutralized organic acids and sulpho organic acids from the treated oil by subjecting the treated oil commingled with the water solution of potassium hydroxide to a temperature of approximately 250 to 280 degrees F. at a pressure of approximately 50 pounds gauge, produced by the introduction of steam into the mixture.
2. That step in the process of purifying mineral lubricating oil stocks after treatment with sulphuric acid and removal of the acid sludge therefrom, comprising, first neutralizing the free mineral acids in the acid treated lubricating oil stock with a watersolutlon of caustic soda introduced in quantitles ust sufiicient to substantially neutralize all free 1 vmineral acids present, without any substantial neutralization of the organic acid emulsifying constituents present, separating and removing the water solution of mineral acid salts from the lubricating oil stock and then commingling the lubricating oil stock from which the free mineral acids have been removed, with a' water solution of potassium hydroxide in quantities sufficient to neutralize the organic acid emulsifying constituents present and thenseparating a water solution of the neutralized organic acid emulsifying constituents from the lubricating oil stock by subjecting the same to a temperature of approximately 250 to 280. degrees F. at a pressureof approximately 50 pounds gauge.
3. That step in the process of purifying mineral lubricating oil stocks after treatment with sulphuric acid and removal of the acid sludge therefrom, comprising, neutralizing the free mineral acids in an acid treated lubricating oil stock with a water solution of caustic soda introduced in quantities just sufficient to substantially neutralize all free mineral acids present and without any substantial neutralization of the organic acid emulsifying constituents contained therein, separating and removing the water solution of mineral acid salts from the lubricating oil stock and then commingling the lubricating oil stock from which the free mineral acids have been removed, with a water solution of potassium hydroxide in quantities sufficient to neutralize all the organic acid emulsifying constituents present, and then separating a water solution of the'neutralized organic acid en1ul- 'sifyin' constituents from the lubricating oil stock y subjecting the same to a temperature of approximately 250 to 280 degrees F. at a pressure of approximately 50 pounds produced by the introduction of steam into the commingled mixture. 7
4. A process of urifying mineral lubrieating oil stocks a ter treatment with sulphuric acid ,,forti'1'e removal of emulsifying constituents, comprising, neutralizing and removing the free mineral acids from an acid treated lubricating oil stockvfrom which the' acid sludge has been substantially removed, with a water solution of caustic soda, without any substantial neutralization or removal of the or anic acid constituents contained therein an then removing the organic acid const1tuents by commingling the said acidtreated lubricating oil stock from which the free mineral acids have been removed, with an ex-' cess of a water solution of potassium hydroxide at a temperature of approximately 250 to 280 F., and finally separating the neutralized organic acids from the lubricating oil stock. r
5. A process; of purifying mineral lubricating.oil stocks after treatment with sulphuric acid,-for the removal of the emulsifyand removing the free mineral acids from an acid treated lubricating oil'stock from which the acid sludge has been substantially removed, with a water solution of caustic soda without any substantial neutralization of the organic acid constituents contained therein and then removing the organic acid constituents by commin ling the acid treated lubricating oil stock rom which the free mineral acids have been removed, with an excess of a water solution of potassium hydroxide and finally separating a water solution containing the neutralized organic acid constituents from the lubricating oil stock at a temperature of approximately 250 to 280 degrees F. and at a pressure of approximately 50 pounds.
6. A process of urifying mineral lubricating oil stocks a er treatment with sulphuric acid and removal of the acid sludge therefrom, comprising, neutralizing the free mineral acids in an acid treated lubricating oil stock, by commingling the same with the requisite quantity of a water solution of sodium hydroxide at a temperature of ap roximately 150 degrees F. without any su stantial neutralization of the organic acid emulsifying constituents contained therein, se arating and removingthe water solution 0 mineral acid salts from the lubricatin oil stock', and then commingling the lubricating oil stock from which the free mineral acids have been removed, with a water solution of potassium hydroxide in quantities suificient to neutralize all the organic acid emulsifying constituents present, and then separating in a water solution containing the neutralized organic acid emulsifyin constituents, from the lubricating oil stock y subjecting the commingled mixture of lubricating oil stock and potassium hydroxide to a temperature of approximately 250 to 280 degrees F. at a pressure of approximately 50 pounds.
In testimony whereof I aflix my signature.
ing constituents, comprising, neutralizing
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US296629A US1761328A (en) | 1928-07-31 | 1928-07-31 | Process of purifying lubricating-oil distillates |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US296629A US1761328A (en) | 1928-07-31 | 1928-07-31 | Process of purifying lubricating-oil distillates |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1761328A true US1761328A (en) | 1930-06-03 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US296629A Expired - Lifetime US1761328A (en) | 1928-07-31 | 1928-07-31 | Process of purifying lubricating-oil distillates |
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| US (1) | US1761328A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2472217A (en) * | 1946-01-19 | 1949-06-07 | Standard Oil Co | Refining hydrocarbon oils |
| US2481816A (en) * | 1947-04-10 | 1949-09-13 | Standard Oil Dev Co | Method of finshing aromatic concentrates |
| US2627496A (en) * | 1950-02-25 | 1953-02-03 | Stratford Eng Corp | Process for washing acid treated distillate |
| US2770581A (en) * | 1953-04-27 | 1956-11-13 | Socony Mobil Oil Co Inc | Stabilization of fuel oil |
| US2868722A (en) * | 1953-10-25 | 1959-01-13 | Socony Mobil Oil Co Inc | Method for producing a stabilized cracked distillate fuel oil |
| US2980606A (en) * | 1956-08-14 | 1961-04-18 | Shell Oil Co | Hydrocarbon refining to reduce sulfur, nitrogen, and naphthenic acid content |
| US20040222128A1 (en) * | 2000-04-25 | 2004-11-11 | Ramesh Varadaraj | Mineral acid enhanced thermal treatment for viscosity reduction of oils (ECB-0002) |
-
1928
- 1928-07-31 US US296629A patent/US1761328A/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2472217A (en) * | 1946-01-19 | 1949-06-07 | Standard Oil Co | Refining hydrocarbon oils |
| US2481816A (en) * | 1947-04-10 | 1949-09-13 | Standard Oil Dev Co | Method of finshing aromatic concentrates |
| US2627496A (en) * | 1950-02-25 | 1953-02-03 | Stratford Eng Corp | Process for washing acid treated distillate |
| US2770581A (en) * | 1953-04-27 | 1956-11-13 | Socony Mobil Oil Co Inc | Stabilization of fuel oil |
| US2868722A (en) * | 1953-10-25 | 1959-01-13 | Socony Mobil Oil Co Inc | Method for producing a stabilized cracked distillate fuel oil |
| US2980606A (en) * | 1956-08-14 | 1961-04-18 | Shell Oil Co | Hydrocarbon refining to reduce sulfur, nitrogen, and naphthenic acid content |
| US20040222128A1 (en) * | 2000-04-25 | 2004-11-11 | Ramesh Varadaraj | Mineral acid enhanced thermal treatment for viscosity reduction of oils (ECB-0002) |
| US7419939B2 (en) * | 2000-04-25 | 2008-09-02 | Exxonmobil Upstream Research Company | Mineral acid enhanced thermal treatment for viscosity reduction of oils (ECB-0002) |
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