US2315530A - Method of sweetening oils - Google Patents

Method of sweetening oils Download PDF

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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
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United States
Prior art keywords
caustic
gasoline
oxygen
sweetening
tannic acid
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Expired - Lifetime
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US404835A
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Vernon J Loyd
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ExxonMobil Oil Corp
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Socony Vacuum Oil Co Inc
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Priority to US404835A priority Critical patent/US2315530A/en
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G27/00Refining of hydrocarbon oils in the absence of hydrogen, by oxidation
    • C10G27/04Refining 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.

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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)
  • 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.
US404835A 1941-07-31 1941-07-31 Method of sweetening oils Expired - Lifetime US2315530A (en)

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Cited By (24)

* Cited by examiner, † Cited by third party
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

Cited By (24)

* Cited by examiner, † Cited by third party
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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