US2626207A - Fuel oil composition - Google Patents

Fuel oil composition Download PDF

Info

Publication number
US2626207A
US2626207A US49848A US4984848A US2626207A US 2626207 A US2626207 A US 2626207A US 49848 A US49848 A US 49848A US 4984848 A US4984848 A US 4984848A US 2626207 A US2626207 A US 2626207A
Authority
US
United States
Prior art keywords
basic
fuel oil
fuel
clogging
sulfonate
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
Application number
US49848A
Inventor
Wies Calmy
John B R Caron
Everett B Glendenning
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shell Development Co
Original Assignee
Shell Development Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shell Development Co filed Critical Shell Development Co
Priority to US49848A priority Critical patent/US2626207A/en
Application granted granted Critical
Publication of US2626207A publication Critical patent/US2626207A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2431Organic compounds containing sulfur, selenium and/or tellurium sulfur bond to oxygen, e.g. sulfones, sulfoxides
    • C10L1/2437Sulfonic acids; Derivatives thereof, e.g. sulfonamides, sulfosuccinic acid esters

Definitions

  • This invention pertains to hydrocarbon fuels, and more particularly to fuel oil compositions capable of preventing or inhibiting the sludging and/or clogging tendencies generally exhibited by hydrocarbon fuels, such as those utilized in burner systems, diesel and combustion engines, and various other industrial and domestic equipment.
  • this invention relates to fuel oil including diesel fuel oil compositions capable of removing preformed deleterious matter from filters, screens, and the like, caused by deterioration and/or presence of foreign bodies (e. g. water) in the fuel oils.
  • Hydrocarbons such as distillate fuels, for example, those having a normal distillation range of from about 300 F. to about 700 F. and particularly from about 340 F. to about 640 F., generally have a marked tendency to deteriorate under oxidizing conditions, and form sludge.
  • Oils Petroleum distillates within the ranges specified and which generally do not exceed 700 F. and preferably are below 675 F. for use :as diesel fuels are further examples of the type of oils whichunder conditions described have a tendency toward screen or filter clogging, particularly when they contain minor amounts of water dispersed therein.
  • n is an integer of from 1 to 5
  • M is a I polyvalent metal
  • X is an element of the group consisting of O, S, Se and Te
  • Y is an acidic portion of the anionic part of the basic salt to which M is linked and is a -S03H radical, wherein the Xs may be the same or different elements from the group consisting of O, S,Se and Te.
  • a minor amount of a detergent l and/or solutizer may also be added to the composition.
  • hydrocarbon distillate fuel oils in which? the active ingredient and/or ingredients of this I invention are dispersed or dissolved may be treated or untreated catalytically cracked fuel oils, or mixtures of cracked fuels with straight run fuel oils, which have an initial distillation point of about 300 F. and an end distillationi point not exceeding 700 F.
  • these 1 fuels have a boiling range-of from about 340 F. to about 700 F., and preferably a boilingrangef, of from about 400 F. to about 675 F; I l
  • Cracked fuels may be obtained by thermal or catalytic cracking of certain petroleum hydrocarbon feed stocks. Both types of cracked fuels, as well as blends of cracked and straight-run fuels, may be acid and/or caustic treated to improve their stability.
  • hydrocarbon distillates which are utilized as bases in compositions of this invention are cracked gas oils, fuel oils, furnace oils, burner oils, diesel fuel oils, kerosene, etc., and mixtures of said cracked fuels with the corresponding or like straight-run hydrocarbon fractions, e. g. fuel oils, etc.
  • Fuel oils which have marked tendencies towards sludging and clogging of screens, filters, etc., are primarily cracked or blends of cracked and straight-run fuel oils which have the following properties:
  • the surface active agents which possess the unique property of inhibiting sludge formation or of removing preformed deposits from surfaces (thereby preventing clogging of systems utilizing fuels normally susceptible of causing such deterioration) are the basic salts of polyvalent metals represented broadly by the partial general formula referred to above.
  • Benzene sulfonic acid Toluene sulfonic acid Triisopropyl naphthalene sulfonic acid Diphenyl sulfonic acid Diwax benzene sulfonic acid Xylene sulfonic acid Benzene disulfonic acid Alkane sulfonic acids, e. g. amyl, octyl, nonyl,
  • Petroleum sulfonic acids are produced bytreating suitable petroleum hydrocarbon fractions with sulfuric acid.
  • a turbine oil having a Saybolt Universal viscosity at 100 F. of from about 400 to 540 seconds is treated with fuming sulfuric acid, preferably in small increments.
  • fuming sulfuric acid preferably in small increments.
  • the sludge which forms is removed and the acid-treated oil containing dissolved oil-soluble sulfonic acids is neutralized with a solution of sodium hydroxide.
  • the aqueous alkali solution is removed from the mixture and the sodium salts of petroleum sulfoniceacid extracted with alcohol.
  • the alcohol layer containing the sulfonates can be removed by distillation or by any other suitable means.
  • the sodium petroleum sulfonate can be converted to the basic metal salt of petroleum sulfonic acid by treating said sodium petroleum sulfonate with calculated amounts of, for example, a mixture of calcium chloride and calcium hydroxide.
  • the reaction may be represented by the following equation:
  • Petroleum sulfonic acids which are particularly preferred are derived from naphthenic, Gulf-Coastal, or Mid-Continent oils.
  • the petroleum sulfonic acids may be obtained by the method described above or by any other means such as those disclosed in the U. S. Patents Nos. 2,388,677, 2,395,713, 2,413,199, 2,413,311, 2,414,773, 2,416,397, and if desired purified by such means as those disclosed in U. S. Patents, Nos. 2,236,933, 2,334,532, 2,357,866, 2,368,452, and 2,406,763, prior to or after the basic salts ofsaid acids have been made.
  • the basic salts may be formed by saponifying any of the acids or acid-forming materials referred to above with an excess of a polyvalent metal compound such as the hydroxides or the like.
  • a preferred method for'forming the basic salts of this invention is to react the desired acidic compound with a polyvalent metal halide or a sulfate and thereafter treating the salt thus formed with metal hydroxide or alcoholate.
  • the basic salt may be made by adding a mixture of the polyvalent metal hydroxide and halide in such proportions and amounts as are sufficient to form the basic salt with a desired organic acidic compound.
  • the metal portion of basic salts of this invention may be any polyvalent metal such as Ca, Ba, Mg, Sr, A1, and mixtures thereof:
  • the part of the basic salt containing the metal may be represented by HXM, wherein X is O, S, Se and Te and M may be any of the following:
  • Petroleum sulfonic acid Triisopropyl naphthalene sulfonic acid Diaryl naphthalene sulfonic acid Diwax benzene sulfonic acid Diwax naphthalene sulfonic acid Benzene disulfonic acid Lauryl sulfonic acid
  • the amount of basic salt used in the base or concentrate fuel oil may vary from about 2% and 25%, and preferably between about 5% and 20% by weight. However, greater or lesser concentrations may be used also.
  • compositions of this invention are preferred to add detergents to compositions of this invention.
  • the function of the detergent agents in compositions of this invention is to act as peptizers, to aid in inhibiting or preventng the settling and adhering of impurities and of sludge to surfaces, and to allow any impurities present or formed to pass through the screen or filter system.
  • Detergents which may be used are alkali, alkaline earth and heavy metal and organic nitrogen base salts of various organicacids.
  • the acidic portion of such detergents may consist of naphthenic acids, aromatic and hydroxy aromatic car- 'boxylic acids, and aliphatic acids, said acids containing if desired, substituent groups, e; g. amino, hydroxide, mercapto, halo and sulfur groups, and the like.
  • substituent groups e
  • substituent groups e
  • substituent groups e
  • substituent groups e
  • e amino, hydroxide, mercapto, halo and sulfur groups
  • phenates, alcohola-tes, carbamates, thiocarbamates, xanthates, etc. may be used.
  • Particularly preferred detergents are the salts of alkyl substituted phenol sulfides, or their selenide and/or their telluride equivalents.
  • These phenolic salts may be represented by the general wherein M is a metal; R and R represent at least one alkyl radical attached to the aromatic ring Ar, the total number of carbon atoms in all of such radicals being at least X is O, S, Se and/or Te; Q is S, Se or Te; and n is an integer of from 1 to 4.
  • These salts may be formed :by treating the phenolic compounds with such metal compounds as Li, Na, K, Cu, Hg, Fe, Mn, Mg, Ca, Ba, Sr, Pb, Ni, Co, Sn, Mo, etc.
  • Alkaline earth metals are particularly preferred because of their solubility in hydrocarbons and their excellent detergent properties.
  • the amount of detergent salt used in the concentrate may vary from between about 5 and 15%, and preferably is kept below In systems wherein substantial amounts of moisture are present, a drying agent may be added which is compatible with the active ingredients of this invention. By tying up most of the free moisture in this manner, the amount thereof which would normally combine with sludgeiorming materials is diminished, thus alleviating a-mos-t aggravating clogging problem.
  • Drying agents which are particularly suited are the glycol-ethers, such as diethylene glycol monomethyl, ethyl, N- and is-opropyl ether, diethylene glycol mono-buty'l ether, diethylene glycol monodecyl ether, etc. also 'dipropylene glycol monoethyl ether, dipropylene glycol mono-isopropyl ether, dipropylene glycol mono-isoamyl ether, diisobutylen i glycol-mono isopropyl ether, ethylene-propylene glycol mono-ethyl ether, ethyleneisobutylene glycol mono-isopropyl ether, etc.
  • glycol-ethers such as diethylene glycol monomethyl, ethyl, N- and is-opropyl ether, diethylene glycol mono-buty'l ether, diethylene glycol monodecyl ether, etc. also 'dipropylene glycol monoeth
  • various alcohols may be used, such as diols having 6 or more carbon atoms in the molecule, e. g. hexylene glycol, decylene glycols, 'cetylene glycol-s, etc. diglycols such as dipropylene glycol, di-butylene glycol, diamylene glycol, ether alcohols and particularly the gycol mono-alkyl ethers, e. g. the cellosolves such Amount, percent wt.
  • diols having 6 or more carbon atoms in the molecule e. g. hexylene glycol, decylene glycols, 'cetylene glycol-s, etc.
  • diglycols such as dipropylene glycol, di-butylene glycol, diamylene glycol, ether alcohols and particularly the gycol mono-alkyl ethers, e. g. the cellosolves such Amount, percent wt.
  • compositions of this invention are generally mixed in amounts 'of one pint or less with from about 250 to about 1000 gallons of fuel oil.
  • one pint of any one of the compositions described above per 250 gallons of fuel would correspond to approximately the following concentration of the active ingredients in the final fuel composi tions:
  • Basic metal salt of an organic acidic compound from about 0.0025% to about 0.005%; detergent (salt of an alkyl phenol sulfide), from zero to 7'- ⁇ about 0.0025% or 0.0042%; drying agent (glycol ether), from zero to about 0.0265%.
  • caustic or aromatic nitrogen compound such as aniline
  • Example I Doped and undoped fuel oils were filtered and then clouded with steam. The fuel compositions or undoped fuel oil were circulated through a screen under a constant head. The oil was pumped from a reservoir into a vertical conduit and allowed to flow by gravity through the creen and decrease in flow rate of the various undoped and doped fuel oils noted after being circulated for 24 hours. The results are tabulated below:
  • compositions of this invention may be added minor amounts of foam inhibitors, such as silicone liquids, e. g. dimcthyl silicon, fiuoro organic compounds, e. g. fluoro paraflins, organic esters of monoand poly-carboxylic acids and mono and polyhydric alcohols, e. g. methyl stearate, 'dioctyl sebacate, dioctyl phthalate, glyceryl mono and dioleate or stearate, etc.
  • foam inhibitors such as silicone liquids, e. g. dimcthyl silicon, fiuoro organic compounds, e. g. fluoro paraflins, organic esters of monoand poly-carboxylic acids and mono and polyhydric alcohols, e. g. methyl stearate, 'dioctyl sebacate, dioctyl phthalate, glyceryl mono and dioleate or stearate, etc.
  • a fuel oil normally susceptible to cause clogging due to the presence of cracked com 8.- w ponents and entrained moisture having incorporated therewith a small amount, sufficient to inhibit said clogging tendencies, of a basic aluminum hydrocarbon sulfonate.
  • a non-clogging fuel oil normally susceptible to cause clogging due to the presence of cracked components and entrained moisture having incorporated therewith from about 0.0025% to about 0.005% of a basic aluminum petroleum sulfonate.
  • a non-clogging fuel oil normally susceptible to cause clogging due to the presence of cracked components and entrained moisture having incorporated therewith from about 0.0025% to about 0.005% of a basic magnesium petroleum sulfonate.
  • a non-clogging fuel oil normally susceptible to cause clogging due to the presence of cracked components and entrained moisture having incorporated therewith from about 0.0025% to about 0.005% of a basic calcium petroleum sulfonate.
  • a fuel oil normally susceptible to cause clogging due to the presence of cracked components and entrained moisture, said fuel oil rendered non-clogging by having incorporated therein one pint of a concentrate consisting essentially of from 10 to 20% of a basic polyvalent metal hydrocarbon sulfonate selected from the group of basic alkaline earth metal hydrocarbon sulfonate and basic aluminum hydrocarbon sulfonate, said concentrate being diluted with from 250 to 1,000 gallons of fuel oil.
  • a fuel oil normally susceptible to cause clogging due to the presence of crack-ed components and entrained moisture having incorporated therewith a small amount, sufficient to inhibit said clogging tendencies, of a basic calcium hydrocarbon sulfonate and a minor amount sufiicient to impart detergency to said composition of normal barium salt of alkyl phenol sulfide.
  • a fuel oil normally susceptible to cause clogging due to the presence of cracked components and. entrained moisture, having incorporated therewith a small amount, suilicient to inhibit said clogging tendencies, of a basic calcium hydrocarbon sulfonate and minor amounts of basic zinc stearate and normal calcium salt of alkyl phenol sulfide.
  • a fuel oil normally susceptible to cause clogging due to the presence of cracked components and entrained moisture, having incorporated therewith a small amount, sufiicient to inhibit said clogging tendencies, of a basic calcium petroleum sulfonate and a minor amount sumcient to impart detergency to said composition of sodium petroleum sulfonate.

Description

Patented Jan. 20, 1953 UNITED STATES PATENT OFFICE FUEL OIL COMPOSITION Calmy Wies, New York, N. Y., and John B. R. Caron, North Plainfield, and Everett B. Glendenning, Cranford, N. J assignors to Shell Development Company, San Francisco, Calif., a
corporation of Delaware No Drawing. Application September 17, 1948, Serial No. 49,848
17 Claims. 1
This invention pertains to hydrocarbon fuels, and more particularly to fuel oil compositions capable of preventing or inhibiting the sludging and/or clogging tendencies generally exhibited by hydrocarbon fuels, such as those utilized in burner systems, diesel and combustion engines, and various other industrial and domestic equipment. In addition, this invention relates to fuel oil including diesel fuel oil compositions capable of removing preformed deleterious matter from filters, screens, and the like, caused by deterioration and/or presence of foreign bodies (e. g. water) in the fuel oils.
Hydrocarbons, such as distillate fuels, for example, those having a normal distillation range of from about 300 F. to about 700 F. and particularly from about 340 F. to about 640 F., generally have a marked tendency to deteriorate under oxidizing conditions, and form sludge.
Also, the presence of impurities in such fuels, such as the presence of moisture, dispersed water, organic and/or inorganic foreign matter, and the like, causes the formation of insoluble products, which tend to settle out and adhere to surfaces with which they come in contact, thereby K in turn, causing clogging or plugging of filters, strainers, screens, conduit lines, and the like, of the equipment in which they are used. This necessitates frequent cleaning and even replacement of parts, thereby markedly decreasing the performance efficiency of various equipment which utilizes such fuel oils.
The problem of screen clogging is-common, particularly in domestic fuel oil systems employing distillate fuel oils produced by distilling or cracking of petroleum which fuels are characterized by their relatively low viscosity and other properties. Fuel oils of this'type generally conform to the specification set forth in Commercial Standards C. S. 12-40 for Nos. 1, 2, and 3, Fuel."
Oils. Petroleum distillates within the ranges specified and which generally do not exceed 700 F. and preferably are below 675 F. for use :as diesel fuels are further examples of the type of oils whichunder conditions described have a tendency toward screen or filter clogging, particularly when they contain minor amounts of water dispersed therein.
Another place where screen clogging and plugging of conduit lines is encountered is in storage tanks for fuel oils, which tanks may be connected to the burner systems or engines, etc.' The stored fuel generally comes in contact with air, moisture, water, etc., which cause formation and precipitation of sludge material which, in
. 2 turn, deposit on and used for protecting the burners or engines which use such oils as the fuel. I
It is an object of this invention to inhibit sludging tendencies of hydrocarbon fuel oils. 'It is nother ob ect of this invention to inhibit sludging and precipitation of contaminants in hydrocarbon distillate fuel oils, and particularly in cracked hydrocarbon fuels. It is still another object of this invention to provide distillate fuel oils, particularly fuel oils obtained by cracking of hydrocarbons, which fuels have excellent performance characteristics with respect to freedom from screen clogging, even after extensive storage under oxidizing conditions and in the presence of water. Still another object of this invention is to provide a distillate fuel oil composition which 7 minor amount, which amount, however, is sufiicient to inhibit said tendencies of a basic salt of" a. polyvalent metal represented by the partial;
general formula:
(-32) 1M(XH) where n is an integer of from 1 to 5, M is a I polyvalent metal, X is an element of the group consisting of O, S, Se and Te; Y is an acidic portion of the anionic part of the basic salt to which M is linked and is a -S03H radical, wherein the Xs may be the same or different elements from the group consisting of O, S,Se and Te. If desired a minor amount of a detergent l and/or solutizer may also be added to the composition.
The hydrocarbon distillate fuel oils in which? the active ingredient and/or ingredients of this I invention are dispersed or dissolved may be treated or untreated catalytically cracked fuel oils, or mixtures of cracked fuels with straight run fuel oils, which have an initial distillation point of about 300 F. and an end distillationi point not exceeding 700 F. Generally, these 1 fuels have a boiling range-of from about 340 F. to about 700 F., and preferably a boilingrangef, of from about 400 F. to about 675 F; I l
clog the screens or filters 1 Cracked fuels may be obtained by thermal or catalytic cracking of certain petroleum hydrocarbon feed stocks. Both types of cracked fuels, as well as blends of cracked and straight-run fuels, may be acid and/or caustic treated to improve their stability. Specifically, hydrocarbon distillates which are utilized as bases in compositions of this invention are cracked gas oils, fuel oils, furnace oils, burner oils, diesel fuel oils, kerosene, etc., and mixtures of said cracked fuels with the corresponding or like straight-run hydrocarbon fractions, e. g. fuel oils, etc.
Fuel oils which have marked tendencies towards sludging and clogging of screens, filters, etc., are primarily cracked or blends of cracked and straight-run fuel oils which have the following properties:
Gravity, API 29-35 A. S. T. M. dist., F.:
IBP 400-500 EBP 600-700 Sulfur percent weight 0.5-1.05 Carbon residue (10% Btms.) percent weight 0.1-0.4 Pour point, F -15 The surface active agents which possess the unique property of inhibiting sludge formation or of removing preformed deposits from surfaces (thereby preventing clogging of systems utilizing fuels normally susceptible of causing such deterioration) are the basic salts of polyvalent metals represented broadly by the partial general formula referred to above.
A. sulfonic acids:
Benzene sulfonic acid Toluene sulfonic acid Triisopropyl naphthalene sulfonic acid Diphenyl sulfonic acid Diwax benzene sulfonic acid Xylene sulfonic acid Benzene disulfonic acid Alkane sulfonic acids, e. g. amyl, octyl, nonyl,
lauryl Dodecyl sulfonic acid Petroleum sulfonic acids derived from various petroleum fraction such as:
Gas oil Kerosene Light oil Turbine oil Mineral lubricating oil Heavy oil Petroleum waxes, e. g.:
, Petrolatum Paraffin wax and mixtures of various hydrocarbon fractions Wax sulfo salicyclic acid Diwax naphthalene sulfonic acids, etc.
Petroleum sulfonic acids are produced bytreating suitable petroleum hydrocarbon fractions with sulfuric acid. 'For example, a turbine oil having a Saybolt Universal viscosity at 100 F. of from about 400 to 540 seconds is treated with fuming sulfuric acid, preferably in small increments. After a calculated amount of sulfuric acid has been added to the oil, the sludge which forms is removed and the acid-treated oil containing dissolved oil-soluble sulfonic acids is neutralized with a solution of sodium hydroxide. The aqueous alkali solution is removed from the mixture and the sodium salts of petroleum sulfoniceacid extracted with alcohol. The alcohol layer containing the sulfonates can be removed by distillation or by any other suitable means.
The sodium petroleum sulfonate can be converted to the basic metal salt of petroleum sulfonic acid by treating said sodium petroleum sulfonate with calculated amounts of, for example, a mixture of calcium chloride and calcium hydroxide. The reaction may be represented by the following equation:
2RSOaNa C3-C1: C8(OH)2 20a SOaR 2NaC1 wherein R is a long chain hydrocarbon.
Petroleum sulfonic acids which are particularly preferred are derived from naphthenic, Gulf-Coastal, or Mid-Continent oils.
' The petroleum sulfonic acids may be obtained by the method described above or by any other means such as those disclosed in the U. S. Patents Nos. 2,388,677, 2,395,713, 2,413,199, 2,413,311, 2,414,773, 2,416,397, and if desired purified by such means as those disclosed in U. S. Patents, Nos. 2,236,933, 2,334,532, 2,357,866, 2,368,452, and 2,406,763, prior to or after the basic salts ofsaid acids have been made.
The basic salts may be formed by saponifying any of the acids or acid-forming materials referred to above with an excess of a polyvalent metal compound such as the hydroxides or the like. A preferred method for'forming the basic salts of this invention is to react the desired acidic compound with a polyvalent metal halide or a sulfate and thereafter treating the salt thus formed with metal hydroxide or alcoholate. Instead of forming the basic salt in stepwise fashion the basic salt may be made by adding a mixture of the polyvalent metal hydroxide and halide in such proportions and amounts as are sufficient to form the basic salt with a desired organic acidic compound.
The metal portion of basic salts of this invention may be any polyvalent metal such as Ca, Ba, Mg, Sr, A1, and mixtures thereof:
The following table gives typical examples of preferred basic metallic salts which are excellent anti-clogging agents in fuels.
The part of the basic salt containing the metal may be represented by HXM, wherein X is O, S, Se and Te and M may be any of the following:
Cation part:
Calcium Barium Magnesium Strontium Aluminum Acid or anion part:
Petroleum sulfonic acid Triisopropyl naphthalene sulfonic acid Diaryl naphthalene sulfonic acid Diwax benzene sulfonic acid Diwax naphthalene sulfonic acid Benzene disulfonic acid Lauryl sulfonic acid The amount of basic salt used in the base or concentrate fuel oil, may vary from about 2% and 25%, and preferably between about 5% and 20% by weight. However, greater or lesser concentrations may be used also.
If desired, and under certain conditions of use, it is preferred to add detergents to compositions of this invention. The function of the detergent agents in compositions of this invention is to act as peptizers, to aid in inhibiting or preventng the settling and adhering of impurities and of sludge to surfaces, and to allow any impurities present or formed to pass through the screen or filter system.
Detergents which may be used are alkali, alkaline earth and heavy metal and organic nitrogen base salts of various organicacids. The acidic portion of such detergents may consist of naphthenic acids, aromatic and hydroxy aromatic car- 'boxylic acids, and aliphatic acids, said acids containing if desired, substituent groups, e; g. amino, hydroxide, mercapto, halo and sulfur groups, and the like. Also phenates, alcohola-tes, carbamates, thiocarbamates, xanthates, etc., may be used.
Particularly preferred detergents are the salts of alkyl substituted phenol sulfides, or their selenide and/or their telluride equivalents. These phenolic salts may be represented by the general wherein M is a metal; R and R represent at least one alkyl radical attached to the aromatic ring Ar, the total number of carbon atoms in all of such radicals being at least X is O, S, Se and/or Te; Q is S, Se or Te; and n is an integer of from 1 to 4.
These salts may be formed :by treating the phenolic compounds with such metal compounds as Li, Na, K, Cu, Hg, Fe, Mn, Mg, Ca, Ba, Sr, Pb, Ni, Co, Sn, Mo, etc. Alkaline earth metals are particularly preferred because of their solubility in hydrocarbons and their excellent detergent properties.
The following are illustrative examples of the above detergent-s: barium tertiary-octyl phenol sulfide, its di'sulfide, barium ditertiary-amyl phenol sulfide, calcium iso-hexadecyl phenol sulfide, magnesium tertiary-amyl phenol sulfide,-cobelt tertiary-amyl phenol sulfide, barium dodecyl salicylate' sulfide, sulfide of the barium saltv of the ethyl ester ofp-hydroxy dithiobenzoic acid, calcium octyl phenol seleni-de, etc. The amount of detergent salt used in the concentrate may vary from between about 5 and 15%, and preferably is kept below In systems wherein substantial amounts of moisture are present, a drying agent may be added which is compatible with the active ingredients of this invention. By tying up most of the free moisture in this manner, the amount thereof which would normally combine with sludgeiorming materials is diminished, thus alleviating a-mos-t aggravating clogging problem.
Drying agents which are particularly suited are the glycol-ethers, such as diethylene glycol monomethyl, ethyl, N- and is-opropyl ether, diethylene glycol mono-buty'l ether, diethylene glycol monodecyl ether, etc. also 'dipropylene glycol monoethyl ether, dipropylene glycol mono-isopropyl ether, dipropylene glycol mono-isoamyl ether, diisobutylen i glycol-mono isopropyl ether, ethylene-propylene glycol mono-ethyl ether, ethyleneisobutylene glycol mono-isopropyl ether, etc. In
stead of the glycol-ethers, various alcohols may be used, such as diols having 6 or more carbon atoms in the molecule, e. g. hexylene glycol, decylene glycols, 'cetylene glycol-s, etc. diglycols such as dipropylene glycol, di-butylene glycol, diamylene glycol, ether alcohols and particularly the gycol mono-alkyl ethers, e. g. the cellosolves such Amount, percent wt.
Broad Preferred Basic metal salt of an organic acid compound,
e. g.: i Basic aluminum sulfonate. Basic calcium sulfonate 10 2O 15 Detergent, e. g.:
Normal alkali petroleum sulfonate 0-10 10 metal salt of alkyl phenol sulfide, etc Drying agent. e. g.: Polyhydric alcohol glycol ethers, etc 0-50 Fuel oil Balance Balance Specific base compositions may be illustrated by the following examples:
Per cent Composition A:
Basic aluminum sulfonate 20 Fuel oil Composition B:
Basic magnesium sulfonate 20 Fuel oil 80 The following table further illustrates suitable anti-clogging base compositions of this invention:
Components: 1
Surface Active Agents- Basic calcium petroleum sulfonate x x x x x Basic zincstearate x Detergents- Normal Ba salt of alkyl phenol sulfide..
Normal Ca salt of alkyl phenol sulfide.-- Normal 0a aJkyl salicylate Na naphthenate Drying Agents-Diethylcne glycol monobutyl ether 1 All of the above compositions are diluted with a hydrocarbon fuel oil in amounts indicated above.
Compositions of this invention are generally mixed in amounts 'of one pint or less with from about 250 to about 1000 gallons of fuel oil. Thus, for example, on a percentage basis of fuel used, one pint of any one of the compositions described above per 250 gallons of fuel would correspond to approximately the following concentration of the active ingredients in the final fuel composi tions:
Basic metal salt of an organic acidic compound, from about 0.0025% to about 0.005%; detergent (salt of an alkyl phenol sulfide), from zero to 7'-\ about 0.0025% or 0.0042%; drying agent (glycol ether), from zero to about 0.0265%.
To inhibit any corrosive tendencies of fuel compositions of this invention a minute amount of caustic or aromatic nitrogen compound, such as aniline, may also be added. These compounds act as alkaline reserves and render the fuel compositions substantially non-corrosive to copper, brass and other metals.
The following examples illustrate the effectiveness of compositions of this invention:
Example I Doped and undoped fuel oils were filtered and then clouded with steam. The fuel compositions or undoped fuel oil were circulated through a screen under a constant head. The oil was pumped from a reservoir into a vertical conduit and allowed to flow by gravity through the creen and decrease in flow rate of the various undoped and doped fuel oils noted after being circulated for 24 hours. The results are tabulated below:
To compositions of this invention may be added minor amounts of foam inhibitors, such as silicone liquids, e. g. dimcthyl silicon, fiuoro organic compounds, e. g. fluoro paraflins, organic esters of monoand poly-carboxylic acids and mono and polyhydric alcohols, e. g. methyl stearate, 'dioctyl sebacate, dioctyl phthalate, glyceryl mono and dioleate or stearate, etc. Compositions of this invention are non-corrosive and do not interfere with the function of the fuel in which they are dispersed.
We claim as our invention:
1. A fuel oil normally susceptible to cause clogging due to thepresence of cracked components and entrained moisture having incorporated therewith a small amount, sufficient to inhibit said clogging tendencies, of a basic polyvalent metal hydrocarbon sulfonate selected from the group of alkaline earth metal hydrocarbon sulfonate and basic aluminum hydrocarbon sulfonate.
2. A fuel oil normally susceptible to cause clo ging due to the presence of cracked components and entrained moisture having incorporated therewith a small amount, sufficient to inhibit said clogging tendencies, of a basic magnesium hydrocarbon sulfonate.
3. A fuel oil normally susceptible to cause clogging due to the presence of cracked components and entrained moisture havin incorporated therewith a small amount, sufficient to inhibit said clogging tendencies, of a basic calcium hydrocarbon sulfonate.
4. A fuel oil normally susceptible to cause clogging due to the presence of cracked com 8.- w ponents and entrained moisture having incorporated therewith a small amount, sufficient to inhibit said clogging tendencies, of a basic aluminum hydrocarbon sulfonate.
5. A non-clogging fuel oil normally susceptible to cause clogging due to the presence of cracked components and entrained moisture having incorporated therewith from about 0.0025% to about 0.005% of a basic aluminum petroleum sulfonate.
6. A non-clogging fuel oil normally susceptible to cause clogging due to the presence of cracked components and entrained moisture having incorporated therewith from about 0.0025% to about 0.005% of a basic magnesium petroleum sulfonate.
'7. A non-clogging fuel oil normally susceptible to cause clogging due to the presence of cracked components and entrained moisture having incorporated therewith from about 0.0025% to about 0.005% of a basic calcium petroleum sulfonate.
8. A fuel oil normally susceptible to cause clogging due to the presence of cracked components and entrained moisture, said fuel oil rendered non-clogging by having incorporated therein one pint of a concentrate consisting essentially of from 10 to 20% of a basic polyvalent metal hydrocarbon sulfonate selected from the group of basic alkaline earth metal hydrocarbon sulfonate and basic aluminum hydrocarbon sulfonate, said concentrate being diluted with from 250 to 1,000 gallons of fuel oil.
9. A fuel oil normally susceptible to cause clogging due to the presence of crack-ed components and entrained moisture, having incorporated therewith a small amount, sufficient to inhibit said clogging tendencies, of a basic calcium hydrocarbon sulfonate and a minor amount sufiicient to impart detergency to said composition of normal barium salt of alkyl phenol sulfide.
10. A fuel oil normally susceptible to cause clogging due to the presence of cracked components and entrained moisture, having incorporated therewith a small amount, sufficient to inhibit said clogging tendencies, of a basic calcium hydrocarbon sulfonate and a minor amount sufficient to impart detergency to said composition of normal calcium alkyl salicylate.
11. A fuel oil normally susceptible to cause clogging due to the presence of cracked components and entrained moisture, having incorporated therewith a small amount, sufficient to inhibit said clogging tendencies, of a basic calcium hydrocarbon sulfonate and a minor amount su fiicient to impart detergency to said composition of sodium naphthenate.
12. A fuel oil normally susceptible to cause clogging due to the presence of cracked components and. entrained moisture, having incorporated therewith a small amount, suilicient to inhibit said clogging tendencies, of a basic calcium hydrocarbon sulfonate and minor amounts of basic zinc stearate and normal calcium salt of alkyl phenol sulfide.
13. A fuel oil normally susceptible to cause clogging due to the presence of cracked com ponents and entrained moisture, having incorporated therewith a small amount, sufiicient to inhibit said clogging tendencies, of a basic calcium petroleum sulfonate and a minor amount sufficient to impart detergency to said composi tion of normal barium salt of alkyl phenol sulfide.
14. A fuel oil normally susceptible to cause clogging due to the presence of cracked components and entrained moisture, having incorporated therewith a small amount, sufficient to inhibit said clogging tendencies, of a basic calcium petroleum sulfonate and a minor amount sufficient to impart detergency to said composition of normal calcium alkyl salicylate.
15. A fuel oil normally susceptible to cause clogging due to the presence of cracked components and entrained moisture, having incorporated therewith a small amount, sufficient to inhibit said clogging tendencies, of a basic calcium petroleum sulfonate and a minor amount sufficient to impart detergency to said composition of sodium naphthenate.
16. A fuel oil normally susceptible to cause clogging due to the presence of cracked components and entrained moisture, having incorporated therewith a small amount, suflicient to inhibit said clogging tendencies, of a basic calcium petroleum sulfonate and minor amounts of basic zinc stearate and normal calcium salt of alkyl phenol sulfide.
17. A fuel oil normally susceptible to cause clogging due to the presence of cracked components and entrained moisture, having incorporated therewith a small amount, sufiicient to inhibit said clogging tendencies, of a basic calcium petroleum sulfonate and a minor amount sumcient to impart detergency to said composition of sodium petroleum sulfonate.
CALMY WIES. JOHN B. R. CARON. EVERETT B. GLENDENNING.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS

Claims (1)

1. A FUEL OIL NORMALLY SUSCEPTIBLE TO CAUSE CLOGGING DUE TO THE PRESENCE OF CRACKED COMPONENTS AND ENTRAINED MOISTURE HAVING INCORPORATED THEREWITH A SMALL AMOUNT, SUFFICIENT TO INHIBIT SAID CLOGGING TENDENCIES, OF A BASIC POLYVALENT METAL HYDROCARBON SULFONATE SELECTED FROM THE GROUP OF ALKALINE EARTH METAL HYDROCARBON SULFONATE AND BASIC ALUMINUM HYDROCARBON SULFONATE.
US49848A 1948-09-17 1948-09-17 Fuel oil composition Expired - Lifetime US2626207A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US49848A US2626207A (en) 1948-09-17 1948-09-17 Fuel oil composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US49848A US2626207A (en) 1948-09-17 1948-09-17 Fuel oil composition

Publications (1)

Publication Number Publication Date
US2626207A true US2626207A (en) 1953-01-20

Family

ID=21962063

Family Applications (1)

Application Number Title Priority Date Filing Date
US49848A Expired - Lifetime US2626207A (en) 1948-09-17 1948-09-17 Fuel oil composition

Country Status (1)

Country Link
US (1) US2626207A (en)

Cited By (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2717826A (en) * 1951-07-25 1955-09-13 Universal Oil Prod Co Stabilization of hydrocarbon distillates
US2866694A (en) * 1950-09-02 1958-12-30 Shell Dev Anti-clogging fuel oil compositions
US2886422A (en) * 1956-06-28 1959-05-12 American Cyanamid Co Hydrocarbon fuels containing sulfonate antifreeze compositions
US2888338A (en) * 1956-09-10 1959-05-26 Exxon Research Engineering Co Rust inhibited stabilized hydrocarbon fuel oil
US2943924A (en) * 1956-05-21 1960-07-05 Gulf Research Development Co Stable fuel oil compositions
US3002825A (en) * 1954-09-14 1961-10-03 Robert S Norris Fuel oil additive for preventing wear in diesel engines and gas turbines
US3002826A (en) * 1955-10-03 1961-10-03 Robert S Norris Fuel oil additive to reduce corrosion and deposits
US3052600A (en) * 1960-06-15 1962-09-04 American Cyanamid Co Stabilized organic phosphate pesticidal compositions in fuel oil
US3061419A (en) * 1958-10-02 1962-10-30 Continental Oil Co Fuel additive for jet propulsion engines
US3105810A (en) * 1959-01-19 1963-10-01 Nalco Chemical Co Preventing fouling of metal conductors in a refinery process
US3109815A (en) * 1958-07-30 1963-11-05 Standard Oil Co Radiation-stable and thermally stable oils
US3306762A (en) * 1965-02-25 1967-02-28 Continental Carbon Co Manufacture of carbon black
US3340030A (en) * 1964-03-27 1967-09-05 Gulf Research Development Co Stabilized fuel oil compositions
US3347633A (en) * 1962-12-31 1967-10-17 Phillips Petroleum Co Carbon black manufacture
US3720615A (en) * 1969-08-11 1973-03-13 Kao Corp Oil-soluble rust preventive composition
EP0240327A2 (en) 1986-03-31 1987-10-07 Exxon Chemical Patents Inc. Cyclic phosphate additives and their use in oleaginous compositions
US4973411A (en) * 1989-09-15 1990-11-27 Texaco Inc. Process for the preparation of sulfurized overbased phenate detergents
WO1999003953A1 (en) * 1997-07-15 1999-01-28 Infineum Usa L.P. Improved fuel oil compositions
US20050258075A1 (en) * 2004-05-14 2005-11-24 Ramesh Varadaraj Viscoelastic upgrading of heavy oil by altering its elastic modulus
US20050258070A1 (en) * 2004-05-14 2005-11-24 Ramesh Varadaraj Fouling inhibition of thermal treatment of heavy oils
US20050263440A1 (en) * 2003-05-16 2005-12-01 Ramesh Varadaraj Delayed coking process for producing free-flowing coke using polymeric additives
US20050269247A1 (en) * 2004-05-14 2005-12-08 Sparks Steven W Production and removal of free-flowing coke from delayed coker drum
US20050279672A1 (en) * 2003-05-16 2005-12-22 Ramesh Varadaraj Delayed coking process for producing free-flowing coke using low molecular weight aromatic additives
US20050279673A1 (en) * 2003-05-16 2005-12-22 Eppig Christopher P Delayed coking process for producing free-flowing coke using an overbased metal detergent additive
US20050284798A1 (en) * 2004-05-14 2005-12-29 Eppig Christopher P Blending of resid feedstocks to produce a coke that is easier to remove from a coker drum
US20100038289A1 (en) * 2008-08-15 2010-02-18 Exxonmobil Research And Engineering Company Metal sulphonate additives for fouling mitigation in petroleum refinery processes

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2141848A (en) * 1938-12-27 Soot remover
US2230642A (en) * 1938-08-13 1941-02-04 Standard Oil Dev Co Fuel oil
US2301795A (en) * 1941-06-16 1942-11-10 Standard Oil Co Stabilizer for oils
US2338578A (en) * 1941-06-21 1944-01-04 Du Pont Heating fuel oil
US2406564A (en) * 1943-05-10 1946-08-27 Standard Oil Dev Co Compounded lubricating oil
US2409687A (en) * 1943-05-10 1946-10-22 Standard Oil Dev Co Sulfur and metal containing compound
US2433716A (en) * 1946-07-12 1947-12-30 Gulf Oil Corp Diesel fuel oils
US2483505A (en) * 1944-12-30 1949-10-04 Standard Oil Dev Co Compounded lubricating oil

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2141848A (en) * 1938-12-27 Soot remover
US2230642A (en) * 1938-08-13 1941-02-04 Standard Oil Dev Co Fuel oil
US2301795A (en) * 1941-06-16 1942-11-10 Standard Oil Co Stabilizer for oils
US2338578A (en) * 1941-06-21 1944-01-04 Du Pont Heating fuel oil
US2406564A (en) * 1943-05-10 1946-08-27 Standard Oil Dev Co Compounded lubricating oil
US2409687A (en) * 1943-05-10 1946-10-22 Standard Oil Dev Co Sulfur and metal containing compound
US2483505A (en) * 1944-12-30 1949-10-04 Standard Oil Dev Co Compounded lubricating oil
US2433716A (en) * 1946-07-12 1947-12-30 Gulf Oil Corp Diesel fuel oils

Cited By (40)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2866694A (en) * 1950-09-02 1958-12-30 Shell Dev Anti-clogging fuel oil compositions
US2717826A (en) * 1951-07-25 1955-09-13 Universal Oil Prod Co Stabilization of hydrocarbon distillates
US3002825A (en) * 1954-09-14 1961-10-03 Robert S Norris Fuel oil additive for preventing wear in diesel engines and gas turbines
US3002826A (en) * 1955-10-03 1961-10-03 Robert S Norris Fuel oil additive to reduce corrosion and deposits
US2943924A (en) * 1956-05-21 1960-07-05 Gulf Research Development Co Stable fuel oil compositions
US2886422A (en) * 1956-06-28 1959-05-12 American Cyanamid Co Hydrocarbon fuels containing sulfonate antifreeze compositions
US2888338A (en) * 1956-09-10 1959-05-26 Exxon Research Engineering Co Rust inhibited stabilized hydrocarbon fuel oil
US3109815A (en) * 1958-07-30 1963-11-05 Standard Oil Co Radiation-stable and thermally stable oils
US3061419A (en) * 1958-10-02 1962-10-30 Continental Oil Co Fuel additive for jet propulsion engines
US3105810A (en) * 1959-01-19 1963-10-01 Nalco Chemical Co Preventing fouling of metal conductors in a refinery process
US3052600A (en) * 1960-06-15 1962-09-04 American Cyanamid Co Stabilized organic phosphate pesticidal compositions in fuel oil
US3347633A (en) * 1962-12-31 1967-10-17 Phillips Petroleum Co Carbon black manufacture
US3340030A (en) * 1964-03-27 1967-09-05 Gulf Research Development Co Stabilized fuel oil compositions
US3306762A (en) * 1965-02-25 1967-02-28 Continental Carbon Co Manufacture of carbon black
US3720615A (en) * 1969-08-11 1973-03-13 Kao Corp Oil-soluble rust preventive composition
EP0240327A2 (en) 1986-03-31 1987-10-07 Exxon Chemical Patents Inc. Cyclic phosphate additives and their use in oleaginous compositions
US4973411A (en) * 1989-09-15 1990-11-27 Texaco Inc. Process for the preparation of sulfurized overbased phenate detergents
WO1999003953A1 (en) * 1997-07-15 1999-01-28 Infineum Usa L.P. Improved fuel oil compositions
US6652609B1 (en) 1997-07-15 2003-11-25 Exxon Chemical Patents Inc Fuel oil compositions
US20050279672A1 (en) * 2003-05-16 2005-12-22 Ramesh Varadaraj Delayed coking process for producing free-flowing coke using low molecular weight aromatic additives
US7658838B2 (en) 2003-05-16 2010-02-09 Exxonmobil Research And Engineering Company Delayed coking process for producing free-flowing coke using polymeric additives
US7645375B2 (en) 2003-05-16 2010-01-12 Exxonmobil Research And Engineering Company Delayed coking process for producing free-flowing coke using low molecular weight aromatic additives
US20050263440A1 (en) * 2003-05-16 2005-12-01 Ramesh Varadaraj Delayed coking process for producing free-flowing coke using polymeric additives
US20050279673A1 (en) * 2003-05-16 2005-12-22 Eppig Christopher P Delayed coking process for producing free-flowing coke using an overbased metal detergent additive
US20050258070A1 (en) * 2004-05-14 2005-11-24 Ramesh Varadaraj Fouling inhibition of thermal treatment of heavy oils
US20050258071A1 (en) * 2004-05-14 2005-11-24 Ramesh Varadaraj Enhanced thermal upgrading of heavy oil using aromatic polysulfonic acid salts
US20050284798A1 (en) * 2004-05-14 2005-12-29 Eppig Christopher P Blending of resid feedstocks to produce a coke that is easier to remove from a coker drum
US20060021907A1 (en) * 2004-05-14 2006-02-02 Ramesh Varadaraj Inhibitor enhanced thermal upgrading of heavy oils
US20060183950A1 (en) * 2004-05-14 2006-08-17 Ramesh Varadaraj Preparation of aromatic polysulfonic acid compositions from light cat cycle oil
US7537686B2 (en) 2004-05-14 2009-05-26 Exxonmobil Research And Engineering Company Inhibitor enhanced thermal upgrading of heavy oils
US7594989B2 (en) * 2004-05-14 2009-09-29 Exxonmobile Research And Engineering Company Enhanced thermal upgrading of heavy oil using aromatic polysulfonic acid salts
US20050269247A1 (en) * 2004-05-14 2005-12-08 Sparks Steven W Production and removal of free-flowing coke from delayed coker drum
US20050258075A1 (en) * 2004-05-14 2005-11-24 Ramesh Varadaraj Viscoelastic upgrading of heavy oil by altering its elastic modulus
US7794586B2 (en) 2004-05-14 2010-09-14 Exxonmobil Research And Engineering Company Viscoelastic upgrading of heavy oil by altering its elastic modulus
US7732387B2 (en) 2004-05-14 2010-06-08 Exxonmobil Research And Engineering Company Preparation of aromatic polysulfonic acid compositions from light cat cycle oil
US7704376B2 (en) * 2004-05-14 2010-04-27 Exxonmobil Research And Engineering Company Fouling inhibition of thermal treatment of heavy oils
US7727382B2 (en) 2004-05-14 2010-06-01 Exxonmobil Research And Engineering Company Production and removal of free-flowing coke from delayed coker drum
WO2010019543A2 (en) * 2008-08-15 2010-02-18 Exxonmobil Research And Engineering Company Metal sulphonate additives for fouling mitigation in petroleum refinery processes
US20100038289A1 (en) * 2008-08-15 2010-02-18 Exxonmobil Research And Engineering Company Metal sulphonate additives for fouling mitigation in petroleum refinery processes
WO2010019543A3 (en) * 2008-08-15 2011-04-21 Exxonmobil Research And Engineering Company Metal sulphonate additives for fouling mitigation in petroleum refinery processes

Similar Documents

Publication Publication Date Title
US2626207A (en) Fuel oil composition
US2684292A (en) Fuel oil composition
US2527987A (en) Fuel oil composition
US2575003A (en) Fuel oil composition
US2548347A (en) Fuel oil composition
US2671758A (en) Colloidal compositions and derivatives thereof
US2553183A (en) Fuel oil composition
US4229309A (en) Magnesium-containing dispersions
US2455659A (en) Oily composition
US3540866A (en) Fuel oil-water composition containing metal oxide
US2524864A (en) Fuel oil composition
US2639227A (en) Anticlogging fuel oil compositions
US3762890A (en) Stabilized polyvalent metal soap composition
US3158647A (en) Quaternary ammonium fatty, phenate and naphthenate salts
US2580274A (en) Lubricant
US2383033A (en) Lubricants
US2672408A (en) Fuel oil composition
US2398202A (en) Anticorrosive
US3247110A (en) Fuel oil and lubricating oil compositions containing metal salts of the mono-amidesof tetrapropenyl succinic acid
US2320392A (en) Anti-ring-sticking lubricant
US2866694A (en) Anti-clogging fuel oil compositions
US2579890A (en) Nonclogging distillate fuel oil
CA3022309C (en) 2-mercaptobenzimidazole derivatives as corrosion inhibitors
US3121059A (en) Compositions of matter having anti-rust properties
US3018172A (en) Aluminum-containing additive for fuel oil compositions and method of preparing the same