US1569870A - Process for refining oils - Google Patents
Process for refining oils Download PDFInfo
- Publication number
- US1569870A US1569870A US584870A US58487022A US1569870A US 1569870 A US1569870 A US 1569870A US 584870 A US584870 A US 584870A US 58487022 A US58487022 A US 58487022A US 1569870 A US1569870 A US 1569870A
- Authority
- US
- United States
- Prior art keywords
- oil
- sulphide
- solution
- sulphur
- water
- 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
Links
- 239000003921 oil Substances 0.000 title description 27
- 238000000034 method Methods 0.000 title description 5
- 238000007670 refining Methods 0.000 title description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 239000005864 Sulphur Substances 0.000 description 9
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 8
- HTUMBQDCCIXGCV-UHFFFAOYSA-N lead oxide Chemical compound [O-2].[Pb+2] HTUMBQDCCIXGCV-UHFFFAOYSA-N 0.000 description 5
- YEXPOXQUZXUXJW-UHFFFAOYSA-N lead(II) oxide Inorganic materials [Pb]=O YEXPOXQUZXUXJW-UHFFFAOYSA-N 0.000 description 5
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 4
- 239000002244 precipitate Substances 0.000 description 4
- 229910052708 sodium Inorganic materials 0.000 description 4
- 239000011734 sodium Substances 0.000 description 4
- 235000011121 sodium hydroxide Nutrition 0.000 description 3
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 229910052783 alkali metal Inorganic materials 0.000 description 2
- 150000001340 alkali metals Chemical class 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- XCAUINMIESBTBL-UHFFFAOYSA-N lead(ii) sulfide Chemical compound [Pb]=S XCAUINMIESBTBL-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910001369 Brass Inorganic materials 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- COOGPNLGKIHLSK-UHFFFAOYSA-N aluminium sulfide Chemical compound [Al+3].[Al+3].[S-2].[S-2].[S-2] COOGPNLGKIHLSK-UHFFFAOYSA-N 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 239000010951 brass Substances 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- ZFXVRMSLJDYJCH-UHFFFAOYSA-N calcium magnesium Chemical compound [Mg].[Ca] ZFXVRMSLJDYJCH-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- SMDQFHZIWNYSMR-UHFFFAOYSA-N sulfanylidenemagnesium Chemical compound S=[Mg] SMDQFHZIWNYSMR-UHFFFAOYSA-N 0.000 description 1
- 150000004763 sulfides Chemical class 0.000 description 1
- 239000001117 sulphuric acid Substances 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 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
- C10G19/00—Refining hydrocarbon oils in the absence of hydrogen, by alkaline treatment
- C10G19/02—Refining hydrocarbon oils in the absence of hydrogen, by alkaline treatment with aqueous alkaline solutions
- C10G19/06—Refining hydrocarbon oils in the absence of hydrogen, by alkaline treatment with aqueous alkaline solutions with plumbites or plumbates
Definitions
- the oil is first preferably treated with sulphuric acid in the, roportion of say, 500 650 pounds of acid per 100. barrels ot foil, sometimes preceded by a water wash.
- the oil may be agitated in the presence of the acid for 15 With the addition of' .aclean, Water white distillate sweet odor.
- the oil u on subsequent tests- Application filed August 28,1922. Serial No. 584,870.
- a step in a process for refining and puri' tying mineral oil consisting in subjecting the oil to the action of alkali metal plumbitc in Water solution, in then removing substantially all the alkali metal plumbite solution from the oil, in then treating the freed oil with a metallic sulphide capable of hydrolyzing in Water to complete the reaction of the plnmbite solution, and in then removing the separated precipitate and sulphide compounds.
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)
- Removal Of Specific Substances (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
Patented 19, 1926.
UNITED STATES 1,569,870 PATENT OFFICE- JACQUE c. MORRELL, or C ICACO, ILLINOIS, ASSIGNOR rho UNIVERSAL OIL rROnuC'rs COMPANY, or CHICAGQ, ILLINOIS, A CORPORATION OF sou rn DAKOTA.
PROCESS FOR BEFINING OILS;
NO Drawing.
' carbon oils with a. high sulphur content produced from a raw oil stock having a high sulphur content.
The practice of using a solution of litharge or lead monoxide in sodium hydroxide in conjunction with sulphur for the removal of sulphur compounds in Oils is well known.
However, the mechanism of the reaction has remained obscure, and therefore, variations and im rovements or departures from this method ave been relatively few.
Heretofore, it has been the ractice to agitate a solution of litharge n sodium 'hydroxide (sodium plumbite) with the oil to be, treated, and after. a period of time to add the flowers of sulphur. the suldphur, a precipitate of lead sulphide is forme There is however, a very objectionable feature under such'a method of treatment. Although not generally known, sulphur is quite soluble in hydrocarbon Oils, and no amountwf subsequent washing with water will remove this sulphur dissolved in the Oil. Sulphur in solution in the oil is extremely objectionable, particularly when used as inotor fuel, since it corrodes various metal parts, espeeially brass and copper.
It isthe purpose of tlii'sinvention to eliminate this objectionable feature by the use water, hydro of various compounds of sulphur, and in'particular such substhnces as -calcium, or magnesium sulphide or aluminum sulphide, which though substantiall insoluble in yze when adde to Water forming recipitates of'the corres onding.hy-
. droxldes as well as hydrogen'su phide.
. According to thepreseiit invention, the oil is first preferably treated with sulphuric acid in the, roportion of say, 500 650 pounds of acid per 100. barrels ot foil, sometimes preceded by a water wash. The oil may be agitated in the presence of the acid for 15 With the addition of' .aclean, Water white distillate sweet odor. The oil u on subsequent tests- Application filed August 28,1922. Serial No. 584,870.
to 20 minutes. This isfollowed. by a water wash for 10 or 15 minutes and an alkali wash such as sodium hydroxide or like substances which are used as a base. gallons of 6-l2 B. caustic soda per 100 barrels of oil treated, I have found to he satisfactory. To the oil is then added sodium plumbite (litharge) dissolved in sodium hy- I d roxide or potassium plumbite in the proportion of say, 5 barrels of 16-30? B. caustic containing from 530 pounds of litharge for each 100 barrels of Oil treated. AfterIagL- tation with the plumbite solution, the latter is removed, and although not necessary, in addition it may be desirable to wash out some of the remaining traces of the plumbitc solution from the oil with water before subsequently adding the sulphide.
This removal of the" plumbite solution,
prior to the adding of the sulphide is a wide departure from the usual practice of addin the sulphur while agitating the oil with the plumbite solution. The reason for this is two-fold. First, the sulphide reacts with the plumbite so lution causing unnecessary waste. Second, 1t has been found in connection with the present invention that when a cracked hydrocarbon oil is treated with so dium plumbite solution, an organic compound of lead soluble in oil is formed.
Upon the addition of a small amount of 11 ide of calcium magnesium or aluminum, .or other metallic sulphide materials in the proportion of say, 4 to20 pounds per '100 barrels of oil, which hydrolyze in water,
a precipitate of lead sulphide is immediately produced.
'The1ead.su1phideis allowed to settle and may even be assisted by special treatment. The sulphide material lswithdrawn from theoil, and the oil is subsequently water washed to remove any traces of the remaining sulphide precipitate or sulphide solution. Aft? er this cleanin Operation, the oil is distilled,
preferably wit the use of steam, reducing high sulphur bearing oils with uniformly 11 0 10o aving a 4 I claim as my invention:
A step in a process for refining and puri' tying mineral oil, consisting in subjecting the oil to the action of alkali metal plumbitc in Water solution, in then removing substantially all the alkali metal plumbite solution from the oil, in then treating the freed oil with a metallic sulphide capable of hydrolyzing in Water to complete the reaction of the plnmbite solution, and in then removing the separated precipitate and sulphide compounds.
. JACQUE C. MORRELL.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US584870A US1569870A (en) | 1922-08-28 | 1922-08-28 | Process for refining oils |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US584870A US1569870A (en) | 1922-08-28 | 1922-08-28 | Process for refining oils |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1569870A true US1569870A (en) | 1926-01-19 |
Family
ID=24339114
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US584870A Expired - Lifetime US1569870A (en) | 1922-08-28 | 1922-08-28 | Process for refining oils |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1569870A (en) |
-
1922
- 1922-08-28 US US584870A patent/US1569870A/en not_active Expired - Lifetime
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