US3068083A - Thermally-stable jet combustion fuels - Google Patents

Thermally-stable jet combustion fuels Download PDF

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US3068083A
US3068083A US830741A US83074159A US3068083A US 3068083 A US3068083 A US 3068083A US 830741 A US830741 A US 830741A US 83074159 A US83074159 A US 83074159A US 3068083 A US3068083 A US 3068083A
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fuel
additive composition
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jet
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Paul Y C Gee
Jr Harry J Andress
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ExxonMobil Oil Corp
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Socony Mobil Oil Co Inc
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    • 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
    • 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
    • C10L1/143Organic compounds mixtures of organic macromolecular compounds with organic non-macromolecular compounds
    • 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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/04Use of additives to fuels or fires for particular purposes for minimising corrosion or incrustation

Definitions

  • This invention relates to jet combustion fuels that are stable at relatively high temperatures. It is more particularly concerned with jet combustion fuels adapted for use in high temperature jet engines and with novel additive compositions therefor.
  • Another object of this invention is to provide stable jet combustion fuels. Another object is to provide a means for stabilizing jet combustion fuels against thermal degradation. A further object is to provide jet combustion fuels having a greatly reduced tendency to foul heat exchange tubes and to plug injection nozzles. A specific object is to provide jet combustion fuels containing an additive composition of certain fuel esters and certain metal deactivating compounds.
  • a more specific object is to provide jet combustion fuels containing certain full esters and aldehyde-amine condensation products of the type of arylidene amines or Schiifs bases.
  • the present invention provides an additive composition comprising between about 1 percent and about percent, by weight of the additive mixture, of a deactivator having the formula:
  • the metal deactivator component of the additive compositions of this invention are aldehyde-amine condensation products of the type of arylidene amines or Schiffs bases having the formula:
  • the ester component of the additive compositions of this invention are the full neutral esters of citric acid, phthalic acid, oxalic acid or azelaic acid.
  • the esterifying alcohols can contain between about 4 carbon and about 20 carbon atoms.
  • Nonlimiting examples of the ester component are tri-n-butyl citrate, di-amyl phthalate, di-hexyl oxalate, di-2-ethyl-hexyl azelate, tri-Z-ethylhexyl citrate, tri-n-decyl citrate, tri-isodecyl citrate, diazelate decyl phthalate, tri(isotridecy1) citrate, di(tridecyl) phthalate, di(isodecyl) oxalate, di(isotridecyl) azelate, di-hexyl decenyl phthalate, tri-octadecenyl citrate, and di-octadecenyl azelate.
  • the esters utilizable herein must be, the full neutral esters. It has been found that the partial esters are ineffective and many have a tendency to develop undesirable, heavy emuls, and
  • the ester component can be made by any of the known methods for preparing esters of carboxylic acids.
  • the esters can be prepared by reacting the alcohol in proper proportions with the acid or with the acid anhydride, with or without the use of catalysts such as a p-toluene sulfonic acid monohydrate.
  • it can be used for various techniques of esterification such as azeotropic distillation, removal of water or the use of applied vacuum. It is to be understood that the particular method used to prepare the ester component is of no importance to the preparation. of the additive compositions of this invention or of jet combustion fuels containing them.
  • the amount of metal deactivator component in the additive composition of this invention can vary between about 1 percent and about 10 percent, by weight, of the additive composition, the balance being the full neutral ester aforedescribed.
  • the additive composition will contain between about 2 percent and about 5 percent by weight, of the metal deactivator component, and an especially preferred composition contains about 4 Weight percent of the metal deactivator component.
  • the hydrocarbon jet fuels that are improved in accordance with this invention are hydrocarbon fractions having an initial boiling point of at least about 100 F. and an end boiling point as high as about 750 F. These fuels can be made up of straight-run distillate fractions, catalytically or thermally cracked (including hydrocracked) distillate fractions, or mixtures of straight-run fuel oil, naphtha, etc. with cracked distillate stocks, alkylate, and the like.
  • the principal properties that characterize the jet fuels is their boiling range. Each fuel will have a boiling range which falls within the aforespecified range.
  • Specifications that define typical specific fuels are MIL-F- 5616, MIL-I-5624-D, MIL-F-25656, MIL-F2524A, MIL-F-25576A, MIL-F-25558B, and MILJ-516lE.
  • the amount of additive composition that is added to the jet combustion fuels will vary between about 0.001 percent and about 1 percent, by weight of the fuel, and preferably between about 0.01 percent and about 0.1.
  • concentration of additive composition will vary between about 2 pounds per thousand barrels of fuel and about 2000 pounds per thousand barrels of fuel, and preferably the concentration will vary between about 25 pounds per thousand barrels of fuel and about 250 pounds per thousand barrels of fuel.
  • the test method used for determining the thermal stability characteristics of aviation turbine fuels is a method developed by the Coordinating Research Council which has published in CRC Report Investigation of Thermal Stability of Aviation Turbine Fuels With CFR Fuel Coker (CRC Project CFA-2-54), July 1957. The method is set forth in detail in Appendix XV of the ASTM Standards on Petroleum Products and Lubricants, November 1957, commencing at page 1059.
  • This method provides a means for measuring the high temperature stability of aviation turbine fuels, using an apparatus known as the CFR Fuel Coker, which subjects the test fuel to temperatures and conditions similar to those occurring in some aviation turbine engines.
  • Fuel is pumped at a rate of about 6 pounds per hour through a preheater section which simulates the hot fuel line sections of the engine as typified by an engine fuel-oil cooler. It then passes through a heated filter section which represents the nozzle area or small fuel passages of the hot section of the engine where fuel degradation products may become trapped.
  • a precision sintered stainless steel filter-in the heated filter section traps fuel degradation products formed during the test. The extent of the build-up is noted as an increased pressure drop across the test filter, and in combination with the deposit condition of the preheater, is used as an assessment of the fuels high-temperature stability.
  • the filter temperature was 500 F. and the preheater tube temperature was 400 F. In each run the test was continued until there was a pressure drop of 25 inches of mercury across .the filter or until a time of 300 minutes had elapsed, whichever occurred first.
  • EXAMPLE 2 Another test was run in the Fuel Coker test using the base fuel defined in Example 1 which contained 28.8 pounds per thousand barrels of fuel of tri(isotridecyl) citrate. Pertinent test results are also set forth in Table I.
  • EXAMPLE 3 The base fuel described in Example 1 containing 1.2 pounds per thousand barrels of fuel of N,N-disalicylaldimine of propylene diamine and 28.8 pounds per thousand barrels of fuel of tri(tridecyl) citrate was subjected to the Fuel Coker test. It will be noted that the additive content of this fuel is a combination of the additives tested in Examples 1 and 2. Pertinent test results are set forth in Table I.
  • An additive composition that consists essentially of between about 1 percent and about 10 percent, by weight of the additive composition, of a deactivator having the formula; 1
  • An additive composition that consists essentially of about 4 percent, by weigh-t of the additive composition, of N,N-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of tri- (tridecyl) citrate.
  • An additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of tri- (isodecyl) citrate.
  • An additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of tri- (Z-ethylhexyl) citrate.
  • An additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicy1aldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of trioctadecenyl citrate.
  • An additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicylaldimine of propylene diamine, and about 96 percent, by Weight of the additive composition, of di- (isotridecyl) phthalate.
  • An additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of di- (isodecyl) phthalate.
  • An additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of di- (isotridecyl) oxalate.
  • An additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of di- (isotridecyl) azelate.
  • a stable jet combustion fuel that consists essentially of a hydrocarbon jet fuel containing between about 2 pounds and about 2000 pounds per thousand barrels of fuel of an additive composition that consists essentially of between about 1 percent and about 10 percent, by weight of the additive composition, of a deactivator having the formula:
  • a stable jet combustion fuel that consists essentially of a hydrocarbon jet fuel containing between about 25 pounds and about 250 pounds per thousand barrels of fuel of an additive composition that consists essentially of between about 2 percent and about 5 percent, by weight of the additive composition, of a deactivator having the formula:
  • a stable jet combustion fuel that consists of a hydrocarbon jet fuel containing between about 25 pounds and about 250 pounds per thousand barrels of fuel of an additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'- disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of tri-(tridecyl) citrate.
  • a stable jet combustion fuel that consists of a hydrocarbon jet fuel containing between about 25 pounds and about 250 pounds per thousand barrels of fuel of an additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disa1icylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of tri(isodecyl) citrate.
  • a stable jet combustion fuel that consists of a hydrocarbon jet fuel containing between about 25 pounds and about 250 pounds per thousand barrels of fuel of an additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of tri(2-ethylhexyl) citrate.
  • a stable jet combustion fuel that consists of a hydrocarbon jet fuel containing between about 25 pounds and about 250 pounds per thousand barrels of fuel of an additive composition that consists essentially of about 4 percent, by weight of the additive composition, of
  • N,N'-disalicylaldimine of propylene diamine and about N,N-disalicylaldimiue of propylene diamine, and about;
  • a stable jet combustion fuel that consists of a hydrocarbon jet fuel containing between about 25 pounds and about 250 pounds per thousand barrels of fuel of an additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of di-(isotridecyl) phthalate.
  • a stable jet combustion fuel that consists of a hydrocarbon jet fuel containing between about 25 pounds and about 250 pounds per thousand barrels of fuel of an additive composition that consists essentially of about 4 percent, by weight of the additive composition, of
  • a stable jetcombustion fuel that consists of a hydrocarbon jet fuel containing between about 25 pounds and about 250 pounds per thousand barrels of fuel of .an additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of

Description

3,58,083 Patented Dec. 11, 1962 3,068,083 THERMALLY-STABLE JET COMBUSTION FUEL Paul Y. C. Gee, Woodhury, and Harry J. Andress, .lr., Pitman, N.J., assignors to Socony Mobil Oil Company,
Inc., a corporation 'of New York No Drawing. Filed July 31, 1959, Ser. No. 830,741 20 Claims. (Cl. 44-70) This invention relates to jet combustion fuels that are stable at relatively high temperatures. It is more particularly concerned with jet combustion fuels adapted for use in high temperature jet engines and with novel additive compositions therefor.
As is well known to those familiar with the art, aviation turbine engines, or jet engines, are operated at extremely high temperatures, particularly in the case of supersonic jet aircraft engines. In order to remove some of the heat and also preheat the incoming fuel, the fuel is subjected to indirect heat exchange with the combustion chamber. Then, when passing through the injection nozzles the incoming fuel is further subjected to high temperature conditions. Many jet fuels have been found to be relatively unstable when subjected to high temperatures. Decomposition products are formed which tend to foul the heat exchange tubes and to cause plug. ging of the injection nozzles. As will readily be appreciated, the use of such fuels results in shortened operational life of the engine and can be a source of hazard in the operation of the jet aircraft. Accordingly, the means of stabilizing such fuels against degradation is highly desirable.
It has now been found that thermally unstable jet combustion fuels can be stabilized against degradation simply and economically. It has been discovered that the addition of a small amount of a mixture of certain full esters and certain metal deactivating compounds will stabilize jet combustion fuels against thermal degradation, thereby minimizing the fouling of heat exchange tubes and the plugging of the filters.
Accordingly, it is an object of this invention to provide stable jet combustion fuels. Another object is to provide a means for stabilizing jet combustion fuels against thermal degradation. A further object is to provide jet combustion fuels having a greatly reduced tendency to foul heat exchange tubes and to plug injection nozzles. A specific object is to provide jet combustion fuels containing an additive composition of certain fuel esters and certain metal deactivating compounds.
A more specific object is to provide jet combustion fuels containing certain full esters and aldehyde-amine condensation products of the type of arylidene amines or Schiifs bases. Other objects and advantages of this invention will become apparent to those skilled in the art from the following detailed description.
In general, the present invention provides an additive composition comprising between about 1 percent and about percent, by weight of the additive mixture, of a deactivator having the formula:
wherein A represents a benzene ring, the OH radical being attached directly to a ring carbon atom ortho to the CH=N- group and R represents an aliphatic radical having the two N atoms attached directly to different carbon atoms of the same open chain of R, and between about 99 percent and about 90 percent, by weight of the additive mixture, of the full neutral aliphatic esters of a polycarboxylic acid selected from the group consisting of citric acid, phthalic acid, oxalic acid, and azelaic acid, wherein the esterifying alcohol contains between about 4 carbon and about carbon atoms; and a jet combustion fuel containing between about 0.001 percent and about 1 percent, by weight, of the said additive composition.
The metal deactivator component of the additive compositions of this invention are aldehyde-amine condensation products of the type of arylidene amines or Schiffs bases having the formula:
wherein A represents a benzene ring, the OH radical being attached directly to a ring carbon atom ortho to the CH=N- group and R represents an aliphatic radical having the two N atoms attached directly to different carbon atoms of the same open chain of R, and between about 99 percent and about percent, by weight, of the additive mixture, of the full neutral aliphatic esters of a polycarboxylic acid selected from the group consisting of citric acid, phthalic acid, oxalic acid, and azelatic acid, wherein the esterifying alcohol contains between about 4 carbon and about 20 carbon atoms.
These materials have been fully described in US. Letters Patents Numbers 2,181,121 and 2,284,267. Generally, they are produced by reacting two moles of salicylaldehyde with one mole of a diamine such as ethylene diamine or propylene diamine with the elimination of two moles of water of condensation. The preferred metal deactivator is the N,N'-disalicylaldimine of propylene diamine having the structure:
| ([3135 l CHNC'HBCHNCH The ester component of the additive compositions of this invention are the full neutral esters of citric acid, phthalic acid, oxalic acid or azelaic acid. The esterifying alcohols can contain between about 4 carbon and about 20 carbon atoms. Nonlimiting examples of the ester component are tri-n-butyl citrate, di-amyl phthalate, di-hexyl oxalate, di-2-ethyl-hexyl azelate, tri-Z-ethylhexyl citrate, tri-n-decyl citrate, tri-isodecyl citrate, diazelate decyl phthalate, tri(isotridecy1) citrate, di(tridecyl) phthalate, di(isodecyl) oxalate, di(isotridecyl) azelate, di-hexyl decenyl phthalate, tri-octadecenyl citrate, and di-octadecenyl azelate. It is to be noted that the esters utilizable herein must be, the full neutral esters. It has been found that the partial esters are ineffective and many have a tendency to develop undesirable, heavy emulsions with water in the fuels.
As will readily be appreciated by those familiar with the art, the ester component can be made by any of the known methods for preparing esters of carboxylic acids. Thus, for example, the esters can be prepared by reacting the alcohol in proper proportions with the acid or with the acid anhydride, with or without the use of catalysts such as a p-toluene sulfonic acid monohydrate. Likewise, it can be used for various techniques of esterification such as azeotropic distillation, removal of water or the use of applied vacuum. It is to be understood that the particular method used to prepare the ester component is of no importance to the preparation. of the additive compositions of this invention or of jet combustion fuels containing them.
The amount of metal deactivator component in the additive composition of this invention can vary between about 1 percent and about 10 percent, by weight, of the additive composition, the balance being the full neutral ester aforedescribed. In preferred practice the additive composition will contain between about 2 percent and about 5 percent by weight, of the metal deactivator component, and an especially preferred composition contains about 4 Weight percent of the metal deactivator component.
' The hydrocarbon jet fuels that are improved in accordance with this invention are hydrocarbon fractions having an initial boiling point of at least about 100 F. and an end boiling point as high as about 750 F. These fuels can be made up of straight-run distillate fractions, catalytically or thermally cracked (including hydrocracked) distillate fractions, or mixtures of straight-run fuel oil, naphtha, etc. with cracked distillate stocks, alkylate, and the like. The principal properties that characterize the jet fuels is their boiling range. Each fuel will have a boiling range which falls within the aforespecified range. Specifications that define typical specific fuels are MIL-F- 5616, MIL-I-5624-D, MIL-F-25656, MIL-F2524A, MIL-F-25576A, MIL-F-25558B, and MILJ-516lE.
' The amount of additive composition that is added to the jet combustion fuels will vary between about 0.001 percent and about 1 percent, by weight of the fuel, and preferably between about 0.01 percent and about 0.1. In terms of weight per unit volume of fuel the concentration of additive composition will vary between about 2 pounds per thousand barrels of fuel and about 2000 pounds per thousand barrels of fuel, and preferably the concentration will vary between about 25 pounds per thousand barrels of fuel and about 250 pounds per thousand barrels of fuel.
The test method used for determining the thermal stability characteristics of aviation turbine fuels is a method developed by the Coordinating Research Council which has published in CRC Report Investigation of Thermal Stability of Aviation Turbine Fuels With CFR Fuel Coker (CRC Project CFA-2-54), July 1957. The method is set forth in detail in Appendix XV of the ASTM Standards on Petroleum Products and Lubricants, November 1957, commencing at page 1059. This method provides a means for measuring the high temperature stability of aviation turbine fuels, using an apparatus known as the CFR Fuel Coker, which subjects the test fuel to temperatures and conditions similar to those occurring in some aviation turbine engines. Fuel is pumped at a rate of about 6 pounds per hour through a preheater section which simulates the hot fuel line sections of the engine as typified by an engine fuel-oil cooler. It then passes through a heated filter section which represents the nozzle area or small fuel passages of the hot section of the engine where fuel degradation products may become trapped. A precision sintered stainless steel filter-in the heated filter section traps fuel degradation products formed during the test. The extent of the build-up is noted as an increased pressure drop across the test filter, and in combination with the deposit condition of the preheater, is used as an assessment of the fuels high-temperature stability. In the testing described herein the filter temperature was 500 F. and the preheater tube temperature was 400 F. In each run the test was continued until there was a pressure drop of 25 inches of mercury across .the filter or until a time of 300 minutes had elapsed, whichever occurred first.
' EXAMPLE 1 A hydrocarbonjet combustion fuel boiling between about 370 F. and about 520 F. was subjected to the .Fuel Coker test. Then another portion of the fuel containing 1.2 pounds per thousand barrels of fuel of N,N-
disalicylaldirnine of propylene diamine was tested. Pertinent test results are set forth in Table I.
EXAMPLE 2 Another test was run in the Fuel Coker test using the base fuel defined in Example 1 which contained 28.8 pounds per thousand barrels of fuel of tri(isotridecyl) citrate. Pertinent test results are also set forth in Table I.
EXAMPLE 3 The base fuel described in Example 1 containing 1.2 pounds per thousand barrels of fuel of N,N-disalicylaldimine of propylene diamine and 28.8 pounds per thousand barrels of fuel of tri(tridecyl) citrate was subjected to the Fuel Coker test. It will be noted that the additive content of this fuel is a combination of the additives tested in Examples 1 and 2. Pertinent test results are set forth in Table I.
It is to be noted that neither the neutral ester nor the metal deactivator was appreciably effective in preventing filter plugging and preheater deposits. On the other hand, the combination of. the two additives was completely effective in both respects.
As has been mentioned hereinbefore combinations of other esters with the metal deactivator are also effective in stabilizing jet combustion fuels. Using the base fuel described in Example 1, a series of blends were prepared in accordance with the present invention and each blend was subjected to the Fuel Coker test. Pertinent data and results of these tests are set forth in Table II. Although the present invention has been described with preferred embodiments, it is to be understood that modifications and variations may be resorted to, without'departing. from the spirit and scope of this invention, as those skilled in the art will readily understand. Such variations and modifications are considered to be within the purview and scope of the appended claims.
What is claimed is:
1. An additive composition that consists essentially of between about 1 percent and about 10 percent, by weight of the additive composition, of a deactivator having the formula; 1
wherein A represents a benzene ring, the OH radical being attached directly to a ring carbon atom ortho'to the CH=N group and R represents an alkylene hydrocarbon radical having the two N atoms attached directly to diiferent'carbon atoms of the same open chain of R; and between about 99 percent and about percent, by weight of the additive composition, of the full neutral ali- =phatic hydrocarbon esters of a polycarboxylic acid selected from the group consisting of citric acid, phthalic acid, oxalic acid, and azelaic acid, wherein the esterifying alcohol contains betweenabout 4 carbon atoms and about l20.carbon atoms.
2.;An additive coposition that consists essentially of between about 2. percent and about 5 percent, by weight Table II Additive Combination Filter Plugging Additive Preheater Combina- Deposits Example Wt. Wt. tion, Cone. Press. at 300 Ester Per- Metal Deaetivator Per- 1b./l,000 Drop Time Min.
cent cent bbls. fuel lngles, Min. Rating Tri-isodeoyl citrate 96 N,N-disalicylaldimine of 4 30 0.0 300 Code 1 propylene diamine. Tri-(Z-ethylhexyl) citrate d 4 30 0.2 300 Code Tri-(n-deeyl) citratc 4 30 0.8 300 Do. Tri-(n-butyl) citrate, 4 30 2. 0 300 Do. Tri-oetadecenyl citrate. 4 30 0.0 300 Do. Di-(isotridecyl) phthalate 4 30 0. 7 300 Do. Di-isodeeyl phthalate 4 30 0. 3 300 Do. Di-(isotridecyl) oxalate 4 30 0.2 300 Code 1 Di-(isotridecyl) azelate 4 30 0.6 300 Code 2 Uninhibited fuel 0 25.0 100 Code 4 of the additive composition, of a deactivator having the formula:
wherein A represents a benzene ring, the OH radical being attached directly to a ring carbon atom ortho to the CH=N- group and R represents an alkylene hydrocarbon radical having the two N atoms attached directly to different carbon atoms of the same open chain of R; and between about 98 percent and about 95 percent, by weight of the additive composition, of the full neutral aliphatic hydrocarbon esters of a polycarboxylic acid selected from the group consisting of citric acid, phthalic acid, oxalic acid, and azelaic acid, wherein the esterifying alcohol contains between about 4 carbon atoms and about carbon atoms.
3. An additive composition that consists essentially of about 4 percent, by weigh-t of the additive composition, of N,N-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of tri- (tridecyl) citrate.
4. An additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of tri- (isodecyl) citrate.
5. An additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of tri- (Z-ethylhexyl) citrate.
6. An additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicy1aldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of trioctadecenyl citrate.
7. An additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicylaldimine of propylene diamine, and about 96 percent, by Weight of the additive composition, of di- (isotridecyl) phthalate.
8. An additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of di- (isodecyl) phthalate.
9. An additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of di- (isotridecyl) oxalate.
10. An additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of di- (isotridecyl) azelate.
11. A stable jet combustion fuel that consists essentially of a hydrocarbon jet fuel containing between about 2 pounds and about 2000 pounds per thousand barrels of fuel of an additive composition that consists essentially of between about 1 percent and about 10 percent, by weight of the additive composition, of a deactivator having the formula:
wherein A represents a benzene ring, the OH radical being attached directly to a ring carbon atom ortho to the -CH=N group and R represents an alkylene hydrocarbon radical having the two N atoms attached directly to different carbon atoms of the same open chain of R; and between about 99 percent and about percent, by weight of the additive composition, of the full neutral aliphatic hydrocarbon esters of a polycarboxylic acid selected from the group consisting of citric acid, phthalic acid, oxalic acid, and azelaic acid, wherein the esterifying alcohol contains between about 4 carbon atoms and about 20 carbon atoms.
12. A stable jet combustion fuel that consists essentially of a hydrocarbon jet fuel containing between about 25 pounds and about 250 pounds per thousand barrels of fuel of an additive composition that consists essentially of between about 2 percent and about 5 percent, by weight of the additive composition, of a deactivator having the formula:
wherein A represents a benzene ring, the OH radical being attached directly to a ring carbon atom ortho to the CH=N- group and R represents an alkylene hydrocarbon radical having the two N atoms attached directly to diiferent carbon atoms of the same open chain of R; and between about 98 percent and about percent, by weight of the additive composition, of the full neutral aliphatic hydrocarbon esters of a polycarboxylic acid selected from the group consisting of citric acid, phthalic acid, oxalic acid, and azelaic acid, wherein the esterifying alcohol contains between about 4 carbon atoms and about 20 carbon atoms.
13. A stable jet combustion fuel that consists of a hydrocarbon jet fuel containing between about 25 pounds and about 250 pounds per thousand barrels of fuel of an additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'- disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of tri-(tridecyl) citrate.
14. A stable jet combustion fuel that consists of a hydrocarbon jet fuel containing between about 25 pounds and about 250 pounds per thousand barrels of fuel of an additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disa1icylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of tri(isodecyl) citrate.
15. A stable jet combustion fuel that consists of a hydrocarbon jet fuel containing between about 25 pounds and about 250 pounds per thousand barrels of fuel of an additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of tri(2-ethylhexyl) citrate.
16. A stable jet combustion fuel that consists of a hydrocarbon jet fuel containing between about 25 pounds and about 250 pounds per thousand barrels of fuel of an additive composition that consists essentially of about 4 percent, by weight of the additive composition, of
, N,N'-disalicylaldimine of propylene diamine, and about N,N-disalicylaldimiue of propylene diamine, and about;
96 percent, by weight of the additive composition, of"
tri-octadecenyl citrate.
17. A stable jet combustion fuel that consists of a hydrocarbon jet fuel containing between about 25 pounds and about 250 pounds per thousand barrels of fuel of an additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of di-(isotridecyl) phthalate.
18. A stable jet combustion fuel that consists of a hydrocarbon jet fuel containing between about 25 pounds and about 250 pounds per thousand barrels of fuel of an additive composition that consists essentially of about 4 percent, by weight of the additive composition, of
96 percent, by weight of the additive composition, of di(isodecyl) phthalate.
19. A stable jetcombustion fuel that consists of a hydrocarbon jet fuel containing between about 25 pounds and about 250 pounds per thousand barrels of fuel of .an additive composition that consists essentially of about 4 percent, by weight of the additive composition, of N,N'-disalicylaldimine of propylene diamine, and about 96 percent, by weight of the additive composition, of
' di(isotridecyl) oxalate. 20. A stable jet combustion fuel that consists of a hy- References Cited in the file of this patent UNITED STATES PATENTS 2,580,005 Cypers et al. Dec. 25, 1951 2,747,979 Thompson May 29, 1956 2,922,706 Durr et al. Jan. 26, 1960 2,993,773 Stromberg July 25, 1961

Claims (1)

11. A STABLE JET COMBUSTION FUEL THAT CONSISTS ESSENTIALLY OF A HYDROCARBON JET FUEL CONTAINING BETWEEN ABOUT 2 POUNDS AND ABOUT 2000 POUNDS PER THOUSAND BARRELS OF FUEL OF AN ADDITIVE COMPOSITION THAT CONSISTS ESSENTIALLY OF BETWEEN ABOUT 1 PERCENT AND ABOUT 10 PERCENT, BY WEIGHT OF THE ADDITIVE COMPOSITION, OF A DEACTIVATOR HAVING THE FORMULA:
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Cited By (14)

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US3419368A (en) * 1967-01-23 1968-12-31 Ashland Oil Inc Thermally stabilized hydrocarbon liquid compositions
US3437583A (en) * 1967-06-13 1969-04-08 Betz Laboratories Anti-foulant agents for petroleum hydrocarbons
US3442791A (en) * 1966-11-17 1969-05-06 Betz Laboratories Anti-foulant agents for petroleum hydrocarbons
US3492219A (en) * 1967-07-17 1970-01-27 Nalco Chemical Co Reducing fouling in refining of petroleum products by salicylidene additive
US3909427A (en) * 1974-09-06 1975-09-30 Phillips Petroleum Co Additives for lubricants and motor fuels
US4113442A (en) * 1974-10-03 1978-09-12 Shell Oil Company Middle distillate fuel compositions
US4749468A (en) * 1986-09-05 1988-06-07 Betz Laboratories, Inc. Methods for deactivating copper in hydrocarbon fluids
US4752374A (en) * 1987-04-20 1988-06-21 Betz Laboratories, Inc. Process for minimizing fouling of processing equipment
US4810354A (en) * 1986-10-31 1989-03-07 Betz Laboratories, Inc. Bifunctional antifoulant compositions and methods
US4847415A (en) * 1988-06-01 1989-07-11 Betz Laboratories, Inc. Methods and composition for deactivating iron in hydrocarbon fluids
US4883580A (en) * 1988-06-01 1989-11-28 Betz Laboratories, Inc. Methods for deactivating iron in hydrocarbon fluids
US5641394A (en) * 1995-04-06 1997-06-24 Nalco/Exxon Energy Chemicals, L.P. Stabilization of hydrocarbon fluids using metal deactivators
WO2010112158A1 (en) * 2009-03-28 2010-10-07 Citrodiesel Gbr Citric acid esters as biogens, regenerative fuels and heating materials
US10221344B2 (en) * 2015-03-23 2019-03-05 Sika Technology Ag Amine for rapid-curing epoxy resin compositions

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US2580005A (en) * 1947-12-31 1951-12-25 Standard Oil Dev Co Extreme pressure lubricating compositions
US2747979A (en) * 1952-11-14 1956-05-29 Eastman Kodak Co Mono-esters of citric acid as metal deactivators for motor fuels
US2922706A (en) * 1957-05-31 1960-01-26 Continental Oil Co Gasoline compositions
US2993773A (en) * 1959-02-02 1961-07-25 Petrolite Corp Ester additives

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2580005A (en) * 1947-12-31 1951-12-25 Standard Oil Dev Co Extreme pressure lubricating compositions
US2747979A (en) * 1952-11-14 1956-05-29 Eastman Kodak Co Mono-esters of citric acid as metal deactivators for motor fuels
US2922706A (en) * 1957-05-31 1960-01-26 Continental Oil Co Gasoline compositions
US2993773A (en) * 1959-02-02 1961-07-25 Petrolite Corp Ester additives

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3442791A (en) * 1966-11-17 1969-05-06 Betz Laboratories Anti-foulant agents for petroleum hydrocarbons
US3419368A (en) * 1967-01-23 1968-12-31 Ashland Oil Inc Thermally stabilized hydrocarbon liquid compositions
US3437583A (en) * 1967-06-13 1969-04-08 Betz Laboratories Anti-foulant agents for petroleum hydrocarbons
US3492219A (en) * 1967-07-17 1970-01-27 Nalco Chemical Co Reducing fouling in refining of petroleum products by salicylidene additive
US3909427A (en) * 1974-09-06 1975-09-30 Phillips Petroleum Co Additives for lubricants and motor fuels
US4113442A (en) * 1974-10-03 1978-09-12 Shell Oil Company Middle distillate fuel compositions
US4749468A (en) * 1986-09-05 1988-06-07 Betz Laboratories, Inc. Methods for deactivating copper in hydrocarbon fluids
US4894139A (en) * 1986-09-05 1990-01-16 Betz Laboratories, Inc. Methods for deactivating copper in hydrocarbon fluids
US4810354A (en) * 1986-10-31 1989-03-07 Betz Laboratories, Inc. Bifunctional antifoulant compositions and methods
US4752374A (en) * 1987-04-20 1988-06-21 Betz Laboratories, Inc. Process for minimizing fouling of processing equipment
US4847415A (en) * 1988-06-01 1989-07-11 Betz Laboratories, Inc. Methods and composition for deactivating iron in hydrocarbon fluids
US4883580A (en) * 1988-06-01 1989-11-28 Betz Laboratories, Inc. Methods for deactivating iron in hydrocarbon fluids
US5641394A (en) * 1995-04-06 1997-06-24 Nalco/Exxon Energy Chemicals, L.P. Stabilization of hydrocarbon fluids using metal deactivators
WO2010112158A1 (en) * 2009-03-28 2010-10-07 Citrodiesel Gbr Citric acid esters as biogens, regenerative fuels and heating materials
US20110232170A1 (en) * 2009-03-28 2011-09-29 Ecobasis Ag Citric acid esters as biogenic, regenerative fuels and heating materials
CN102378809A (en) * 2009-03-28 2012-03-14 埃科巴希斯股份公司 Citric acid esters as biogens, regenerative fuels and heating materials
US10221344B2 (en) * 2015-03-23 2019-03-05 Sika Technology Ag Amine for rapid-curing epoxy resin compositions

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