US2315530A - Method of sweetening oils - Google Patents
Method of sweetening oils Download PDFInfo
- Publication number
- US2315530A US2315530A US404835A US40483541A US2315530A US 2315530 A US2315530 A US 2315530A US 404835 A US404835 A US 404835A US 40483541 A US40483541 A US 40483541A US 2315530 A US2315530 A US 2315530A
- Authority
- US
- United States
- Prior art keywords
- caustic
- gasoline
- oxygen
- sweetening
- tannic acid
- 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
- 238000000034 method Methods 0.000 title description 10
- 239000003921 oil Substances 0.000 title description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 35
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical class S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 12
- 235000011121 sodium hydroxide Nutrition 0.000 description 12
- TUSDEZXZIZRFGC-UHFFFAOYSA-N 1-O-galloyl-3,6-(R)-HHDP-beta-D-glucose Natural products OC1C(O2)COC(=O)C3=CC(O)=C(O)C(O)=C3C3=C(O)C(O)=C(O)C=C3C(=O)OC1C(O)C2OC(=O)C1=CC(O)=C(O)C(O)=C1 TUSDEZXZIZRFGC-UHFFFAOYSA-N 0.000 description 9
- 239000001263 FEMA 3042 Substances 0.000 description 9
- LRBQNJMCXXYXIU-PPKXGCFTSA-N Penta-digallate-beta-D-glucose Natural products OC1=C(O)C(O)=CC(C(=O)OC=2C(=C(O)C=C(C=2)C(=O)OC[C@@H]2[C@H]([C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)O2)OC(=O)C=2C=C(OC(=O)C=3C=C(O)C(O)=C(O)C=3)C(O)=C(O)C=2)O)=C1 LRBQNJMCXXYXIU-PPKXGCFTSA-N 0.000 description 9
- LRBQNJMCXXYXIU-NRMVVENXSA-N tannic acid Chemical compound OC1=C(O)C(O)=CC(C(=O)OC=2C(=C(O)C=C(C=2)C(=O)OC[C@@H]2[C@H]([C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)O2)OC(=O)C=2C=C(OC(=O)C=3C=C(O)C(O)=C(O)C=3)C(O)=C(O)C=2)O)=C1 LRBQNJMCXXYXIU-NRMVVENXSA-N 0.000 description 9
- 229940033123 tannic acid Drugs 0.000 description 9
- 235000015523 tannic acid Nutrition 0.000 description 9
- 229920002258 tannic acid Polymers 0.000 description 9
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 8
- 239000005864 Sulphur Substances 0.000 description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 8
- 239000003518 caustics Substances 0.000 description 8
- 239000001301 oxygen Substances 0.000 description 8
- 229910052760 oxygen Inorganic materials 0.000 description 8
- 239000000463 material Substances 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 5
- 239000007864 aqueous solution Substances 0.000 description 4
- 239000003153 chemical reaction reagent Substances 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 235000009508 confectionery Nutrition 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 239000003208 petroleum Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- FERIUCNNQQJTOY-UHFFFAOYSA-N Butyric acid Chemical class CCCC(O)=O FERIUCNNQQJTOY-UHFFFAOYSA-N 0.000 description 1
- 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 1
- 239000012190 activator Substances 0.000 description 1
- 229910000288 alkali metal carbonate Inorganic materials 0.000 description 1
- 150000008041 alkali metal carbonates Chemical class 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 150000003868 ammonium compounds Chemical class 0.000 description 1
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical class OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000005504 petroleum refining Methods 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 235000013824 polyphenols Nutrition 0.000 description 1
- 235000011118 potassium hydroxide Nutrition 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229920001864 tannin Polymers 0.000 description 1
- 235000018553 tannin Nutrition 0.000 description 1
- 239000001648 tannin 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
- C10G27/00—Refining of hydrocarbon oils in the absence of hydrogen, by oxidation
- C10G27/04—Refining of hydrocarbon oils in the absence of hydrogen, by oxidation with oxygen or compounds generating oxygen
Definitions
- This invention has to do with the sweetening of petroleum hydrocarbons containing sour sulphur constituents, as mercaptans and the like, to render the material sweet to the doctor test.
- the objective is to remove materials of the nature of dissolved sulphur, hydrogen sulphide, mercaptans or the like or to convert them to innocuous compounds. Washing with aqueous solutions of strong alkalies, such as caustic soda will remove most of the hydrogen sulphide and some, but not all. of the mercaptans. Washing with aqueous caustic to which some material has been added as a "solutizer, or solubility promoter, enables the caustic to dissolve and remove more or all of the mercaptans. Butylene glycols, butyric acids, and phenolic materials are so used.
- Older methods make use of sodium plumbite formed by dissolving lithage in caustic soda, the eiiect here being to convert mercaptan to mercaptides and I later to disulphides, which are innocuous to the doctor test, by addition of free sulphur.
- the principal object of this invention is the provision of a novel process for rendering petroleum hydrocarbons sweet to the doctor test and reducing the amount of mercaptan sulphur.
- This invention is based upon the discovery that efiective reduction of mercaptan sulphur may be eifected by treatment with aqueous caustic soda solution, containing tannic acid, in the presence of oxygen or an oxygen containing gas, such as air.
- the caustic alkali solution to be used may be any of the usual alkaline solutions normally used for these purposes, such as caustic soda, caustic potash, alkali metal carbonates, ammonia and basic ammonium compounds and the like. Usual preference is had for caustic soda, in aqueous solutions of from about 5 Baum to 20 Baum, the usual and preferred strength being around 10 Baum.
- the tannic acid used may be the usual commercial grade of the material.
- this tannic acid activator to be eflfective in quite small amounts, ranging from 5.0% downward to fractions of 1% with amounts of from about 0.3% to about 1.0% by weight of caustic solution being the most effective.
- That method of removing mercaptans from of the reagent. gasoline and the like comprising contacting the I claim: 35 oil in the presence of oxygen-with an aqueous 1.
- That method of removing mercaptans from solution of caustic soda activated by the addition petroleum fractions comprising contacting the of a small amount, less than about 5%, of tannic fraction with an aqueous alkaline reagent to acid. which tannic acid has been added, in the pres- 4.
- That method of removing mercaptans from ence of oxygen. 40 comprising contacting the 2.
- That method of removing mercaptans from gasoline and the like comprising contacting the oil in the presence of oxygen with an aqueous solution of caustic soda activated by the addition of a small amount of tannic acid.
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)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
Patented Apr. 6, 1943 METHOD OF "SWEETENING OILS Vernon J. Loyd, East Chicago, Ind., assignor to Socony-Vacuum Oil Company, Incorporated, New York, N. Y., a corporation of New York No Drawing. Application July 31, 1941, Serial No. 404,835
4 Claims.
This invention has to do with the sweetening of petroleum hydrocarbons containing sour sulphur constituents, as mercaptans and the like, to render the material sweet to the doctor test.
In treating hydrocarbons, such as straight run gasoline, natural gasoline, cracked gasoline and the like, to render them sweet to the "doctor test,
the objective is to remove materials of the nature of dissolved sulphur, hydrogen sulphide, mercaptans or the like or to convert them to innocuous compounds. Washing with aqueous solutions of strong alkalies, such as caustic soda will remove most of the hydrogen sulphide and some, but not all. of the mercaptans. Washing with aqueous caustic to which some material has been added as a "solutizer, or solubility promoter, enables the caustic to dissolve and remove more or all of the mercaptans. Butylene glycols, butyric acids, and phenolic materials are so used. Older methods make use of sodium plumbite formed by dissolving lithage in caustic soda, the eiiect here being to convert mercaptan to mercaptides and I later to disulphides, which are innocuous to the doctor test, by addition of free sulphur.
In general, all processes of this kind leave something to be desired, and this field, one of the oldest in petroleum refining, is still the subject of active research,
The principal object of this invention is the provision of a novel process for rendering petroleum hydrocarbons sweet to the doctor test and reducing the amount of mercaptan sulphur.
This invention is based upon the discovery that efiective reduction of mercaptan sulphur may be eifected by treatment with aqueous caustic soda solution, containing tannic acid, in the presence of oxygen or an oxygen containing gas, such as air.
In this operation, the reaction is apparently not parallel to the usual solutizer type of operation, since the reaction apparently does not take place to any great extent in the absence of oxygen.
The caustic alkali solution to be used may be any of the usual alkaline solutions normally used for these purposes, such as caustic soda, caustic potash, alkali metal carbonates, ammonia and basic ammonium compounds and the like. Usual preference is had for caustic soda, in aqueous solutions of from about 5 Baum to 20 Baum, the usual and preferred strength being around 10 Baum.
The tannic acid used may be the usual commercial grade of the material.
We have found this tannic acid activator to be eflfective in quite small amounts, ranging from 5.0% downward to fractions of 1% with amounts of from about 0.3% to about 1.0% by weight of caustic solution being the most effective.
To avoid undue consumption of reagent it is best to caustic wash the oil, prior to this treatment, as with an aqueous alkaline reagent, to to remove hydrogen sulphide and the more readily removable sulphur containing materials.
The folowing experimental data show the efiectiveness'of the process herein described. To secure this data straight run and cracked gasolines were treated with various caustic alkali solutions, with and without tannic acid, in various concentrations, with oxygen present, with air, and with nitrogen to show the effect of oxygen elimination.
That: I
Eflect of tannic acid on removal of mercaptan sulphur from straight run gasoline by caustic solution [Raw 8. R. gasoline 0.005% RSH] Gas Number Mercap- NaOH Tanmc Temper- Ratio 0 atmosoi extan Kind B6 acid ature (N aOH.Gaso.) phem "actions removal Per cent F. Per cent 0. 3 100 1:4 All--- l 72. 5 1.0 100 1:4 A112--- 1 a 72. b 5. 0 100 1:4 Lin--- 1 07. 5 0. 0 100 1:4 AIL--. l 25. 0 1. 0 82 1:4 A111--- 3 75. 0 0.0 1:4 NI.-. 1 29.0 0. 0 90 1:4 01.... l 20. 0 1.0 90 1:4 Nu-.- 1 31.8 1. 0 90 1:4 0|..... 1 73. 4 5. 0 90 1:4 01..... 1 02- 5 mm. II
E'fiect of tannic acid on removal of mercaptan sulphur from cracked gasoline by caustic solotion [Thermal cracked gasoline 0.025%ZRSH1 Gas Number Merm NaOH kind Tannin Temper- Rat1o atmos ofex A? tan B. ac1d ature (NaOH.Gaso.) phere actions whom Per cent F. Per cent Fres'n10.3 0.0 100 114 A112... 1 5 Do 0:3 100 1.4 1111-... 1 D 1.0 100 1.4 1411.... 1 31,g Regeneration l 7 (epprox.) 0.0 95 1:4 1 60,2 Regeneration 1 NaOH solu. boiled before using. with).
The above data demonstrate the effectiveness 3. That method of removing mercaptans from of the reagent. gasoline and the like comprising contacting the I claim: 35 oil in the presence of oxygen-with an aqueous 1. That method of removing mercaptans from solution of caustic soda activated by the addition petroleum fractions comprising contacting the of a small amount, less than about 5%, of tannic fraction with an aqueous alkaline reagent to acid. which tannic acid has been added, in the pres- 4. That method of removing mercaptans from ence of oxygen. 40 gasoline and the like comprising contacting the 2. That method of removing mercaptans from gasoline and the like comprising contacting the oil in the presence of oxygen with an aqueous solution of caustic soda activated by the addition of a small amount of tannic acid.
oil in the presence of oxygen with an aqueous solution of caustic soda activated by the addition of a small amount, from about 0.3% to about 1.0%, of tannic acid.
VERNON J. LOYD.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US404835A US2315530A (en) | 1941-07-31 | 1941-07-31 | Method of sweetening oils |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US404835A US2315530A (en) | 1941-07-31 | 1941-07-31 | Method of sweetening oils |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2315530A true US2315530A (en) | 1943-04-06 |
Family
ID=23601248
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US404835A Expired - Lifetime US2315530A (en) | 1941-07-31 | 1941-07-31 | Method of sweetening oils |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2315530A (en) |
Cited By (24)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2425414A (en) * | 1944-08-26 | 1947-08-12 | Pure Oil Co | Regeneration of spent caustic solutions for treating gasoline |
| US2426087A (en) * | 1944-06-26 | 1947-08-19 | Shell Dev | Conversion of hydrosulfides to neutral sulfur substances |
| US2427250A (en) * | 1944-12-06 | 1947-09-09 | Pure Oil Co | Sweetening of hydrocarbon liquids |
| US2431920A (en) * | 1944-12-21 | 1947-12-02 | Shell Dev | Catalytic treatment of sulfurbearing hydrocarbon distillates |
| US2432301A (en) * | 1944-06-26 | 1947-12-09 | Shell Dev | Conversion of hydrosulfides to neutral sulfur compounds |
| US2439670A (en) * | 1945-08-23 | 1948-04-13 | Texas Co | Process for removing acid components from organic liquids |
| US2446507A (en) * | 1945-01-26 | 1948-08-03 | Socony Vacuum Oil Co Inc | Method of removing mercaptans from a liquid mixture of hydrocarbons containing low-boiling and high-boiling mercaptans |
| US2451817A (en) * | 1944-06-26 | 1948-10-19 | Shell Dev | Process for regenerating spent aqueous alkaline solution |
| US2453067A (en) * | 1943-06-11 | 1948-11-02 | Socony Vacuum Oil Co Inc | Method for reducing the mercaptan sulfur content of hydrocarbon oils |
| US2457635A (en) * | 1945-10-10 | 1948-12-28 | Pure Oil Co | Method of regenerating aqueous alkali solution used to extract weakly acidic sulfur compounds from hydrocarbon fluids |
| US2457975A (en) * | 1944-03-09 | 1949-01-04 | Standard Oil Co | Removing mercaptans |
| US2464576A (en) * | 1946-04-18 | 1949-03-15 | Standard Oil Co | Process for the removal of mercaptans from petroleum distillates with an aqueous alkaline reagent containing lignin and the regeneration of the spent alkaline reagent |
| US2467355A (en) * | 1945-03-08 | 1949-04-12 | Socony Vacuum Oil Co Inc | Refining of alkyl phenols |
| US2468701A (en) * | 1945-01-25 | 1949-04-26 | Socony Vacuum Oil Co Inc | Removal of hydrogen sulfide from oils |
| US2516837A (en) * | 1943-06-11 | 1950-08-01 | Socony Vacuum Oil Co Inc | Process of regenerating an aqueous alkali solution |
| US2535833A (en) * | 1946-04-25 | 1950-12-26 | Pure Oil Co | Catalytic oxidation of mercaptans |
| US2550905A (en) * | 1944-07-20 | 1951-05-01 | Standard Oil Co | Mercaptan removal |
| US2574525A (en) * | 1944-03-04 | 1951-11-13 | Pure Oil Co | Regeneration of spent alkali |
| US2583136A (en) * | 1944-09-23 | 1952-01-22 | Pure Oil Co | Process of regenerating an aqueous alkali metal hydroxide solution |
| US2583083A (en) * | 1946-02-13 | 1952-01-22 | Pure Oil Co | Oxidation of acidic sulfur compounds |
| US2600465A (en) * | 1946-02-14 | 1952-06-17 | Pure Oil Co | Method of oxidizing acidic sulfur compounds of the type which occur in hydrocarbon oil |
| US2606099A (en) * | 1943-06-11 | 1952-08-05 | Socony Vacuum Oil Co Inc | Regeneration of alkaline solutions used in the removal of sulfur contaminants from hydrocarbon oils |
| US2701784A (en) * | 1944-04-06 | 1955-02-08 | Socony Vacuum Oil Co Inc | Refining petroleum fractions |
| US2760909A (en) * | 1944-04-15 | 1956-08-28 | Shell Dev | Process for the regeneration of caustic alkali solutions containing mercaptans |
-
1941
- 1941-07-31 US US404835A patent/US2315530A/en not_active Expired - Lifetime
Cited By (24)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2453067A (en) * | 1943-06-11 | 1948-11-02 | Socony Vacuum Oil Co Inc | Method for reducing the mercaptan sulfur content of hydrocarbon oils |
| US2516837A (en) * | 1943-06-11 | 1950-08-01 | Socony Vacuum Oil Co Inc | Process of regenerating an aqueous alkali solution |
| US2606099A (en) * | 1943-06-11 | 1952-08-05 | Socony Vacuum Oil Co Inc | Regeneration of alkaline solutions used in the removal of sulfur contaminants from hydrocarbon oils |
| US2574525A (en) * | 1944-03-04 | 1951-11-13 | Pure Oil Co | Regeneration of spent alkali |
| US2457975A (en) * | 1944-03-09 | 1949-01-04 | Standard Oil Co | Removing mercaptans |
| US2701784A (en) * | 1944-04-06 | 1955-02-08 | Socony Vacuum Oil Co Inc | Refining petroleum fractions |
| US2760909A (en) * | 1944-04-15 | 1956-08-28 | Shell Dev | Process for the regeneration of caustic alkali solutions containing mercaptans |
| US2432301A (en) * | 1944-06-26 | 1947-12-09 | Shell Dev | Conversion of hydrosulfides to neutral sulfur compounds |
| US2451817A (en) * | 1944-06-26 | 1948-10-19 | Shell Dev | Process for regenerating spent aqueous alkaline solution |
| US2426087A (en) * | 1944-06-26 | 1947-08-19 | Shell Dev | Conversion of hydrosulfides to neutral sulfur substances |
| US2550905A (en) * | 1944-07-20 | 1951-05-01 | Standard Oil Co | Mercaptan removal |
| US2425414A (en) * | 1944-08-26 | 1947-08-12 | Pure Oil Co | Regeneration of spent caustic solutions for treating gasoline |
| US2583136A (en) * | 1944-09-23 | 1952-01-22 | Pure Oil Co | Process of regenerating an aqueous alkali metal hydroxide solution |
| US2427250A (en) * | 1944-12-06 | 1947-09-09 | Pure Oil Co | Sweetening of hydrocarbon liquids |
| US2431920A (en) * | 1944-12-21 | 1947-12-02 | Shell Dev | Catalytic treatment of sulfurbearing hydrocarbon distillates |
| US2468701A (en) * | 1945-01-25 | 1949-04-26 | Socony Vacuum Oil Co Inc | Removal of hydrogen sulfide from oils |
| US2446507A (en) * | 1945-01-26 | 1948-08-03 | Socony Vacuum Oil Co Inc | Method of removing mercaptans from a liquid mixture of hydrocarbons containing low-boiling and high-boiling mercaptans |
| US2467355A (en) * | 1945-03-08 | 1949-04-12 | Socony Vacuum Oil Co Inc | Refining of alkyl phenols |
| US2439670A (en) * | 1945-08-23 | 1948-04-13 | Texas Co | Process for removing acid components from organic liquids |
| US2457635A (en) * | 1945-10-10 | 1948-12-28 | Pure Oil Co | Method of regenerating aqueous alkali solution used to extract weakly acidic sulfur compounds from hydrocarbon fluids |
| US2583083A (en) * | 1946-02-13 | 1952-01-22 | Pure Oil Co | Oxidation of acidic sulfur compounds |
| US2600465A (en) * | 1946-02-14 | 1952-06-17 | Pure Oil Co | Method of oxidizing acidic sulfur compounds of the type which occur in hydrocarbon oil |
| US2464576A (en) * | 1946-04-18 | 1949-03-15 | Standard Oil Co | Process for the removal of mercaptans from petroleum distillates with an aqueous alkaline reagent containing lignin and the regeneration of the spent alkaline reagent |
| US2535833A (en) * | 1946-04-25 | 1950-12-26 | Pure Oil Co | Catalytic oxidation of mercaptans |
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