US3421867A - Saturated aliphatic hydrocarbon gasoline - Google Patents

Saturated aliphatic hydrocarbon gasoline Download PDF

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US3421867A
US3421867A US531350A US3421867DA US3421867A US 3421867 A US3421867 A US 3421867A US 531350 A US531350 A US 531350A US 3421867D A US3421867D A US 3421867DA US 3421867 A US3421867 A US 3421867A
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fuel
ron
octane
saturated aliphatic
per gallon
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Robert Y Heisler
Kenneth L Dille
Marc F Fontaine
George W Eckert
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Texaco Inc
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    • GPHYSICS
    • G02OPTICS
    • G02BOPTICAL ELEMENTS, SYSTEMS OR APPARATUS
    • G02B21/00Microscopes
    • G02B21/02Objectives
    • G02B21/025Objectives with variable magnification
    • 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
    • C10L1/18Organic compounds containing oxygen
    • C10L1/185Ethers; Acetals; Ketals; Aldehydes; Ketones
    • C10L1/1857Aldehydes; Ketones
    • 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
    • C10L1/18Organic compounds containing oxygen
    • C10L1/19Esters ester radical containing compounds; ester ethers; carbonic acid esters

Definitions

  • This invention relates to hydrocarbon fuel compositions of high octane rating. More specifically, it involves the discovery that the octane rating of leaded saturated aliphatic fuels having .a minimum Research Octane Number is substantiallly improved by the addition of prescribed concentrations of an oxygentated hydrocarbon compound.
  • Catalytic cracking and catalytic reforming which are the most widely used refining operations in the production of high octane fuels, produce substantial quantities of aromatics; catalytic crac ting also produces a substantial amount of olefins.
  • olefinsand aromatics although possessing high octane ratings, have a poorer response to organo-lead compounds such as tetraethyl lead than saturated aliphatic gasoline components. Accordingly, as the aromatic and olefinic content of the gasolines have increased to meet the octane levels required by modern automotive high compression engines, the lead response of the resulting fuels has diminished. Stated another way, the cctane increment obtained by the addition of an organo-lead compound decreases as the aromatic and olefin cot'ttents of the base fuel increase.
  • the subject invention is a C-I-P of application S.N. 847,086 filed on Oct. 19, 1959. which is an extension of the discovery that hydrocarbyl monocarboxylic acids, certain derivatives and precursors therof have an octane appreciating action in leaded fuels having a minimum concentration of aromatics and/or olefin hydrocarbons.
  • hydrocarbyl monocarboxylic acids in concentrations of the order of 0.1 to 5.0 volume percent and preferably between 0.2 and 2.0 volume percent, act as octane appreciators in leaded fuels having a minimum aromatic and/or olefinic content of the order of 10 percent.
  • Ser. No. 699.944 filed Dec. 2, i957 and its C-l-P
  • Ser No. 743,001 filed June I9, 1958 in the names of G. W. Eckert, and H. V. Hess and E. C.
  • the high octane hydrocarbon motor fuel of this invention consists essentially of saturated aliphatic hydro carbons, an organo'lead anti-knock agent, said saturated aliphatic hydrocarbons having a-minimum RON with i 3 cc. of tetraethyl lead (TEL) per gallon of 102, and
  • an oxygenated hydrocarbon which is either a hydrocarbyl monocarboxylic acid containing 1-30 carbon atoms, a t-alkyl ester of said hydrocarbyl monocarboxylic acid, or a hydrocarbyl aldehyde containing 2-30 carbon atoms.
  • an oxygenated hydrocarbon which is either a hydrocarbyl monocarboxylic acid containing 1-30 carbon atoms, a t-alkyl ester of said hydrocarbyl monocarboxylic acid, or a hydrocarbyl aldehyde containing 2-30 carbon atoms.
  • hydrocarbyl monocarboxylic acids, t-alkyl esters thereof and hydrocarbyl aldehydes substantially improve the carbon fuel having the prescribed minimum RON with 3 cc. of tetraethyl lead per gallon of 102.
  • the reason for the ineffectiveness of these agents in saturated parafiinic fuels of octane rating below the prescribed minimum and their effectiveness in such fuels above the prescribed octane level is currently the subject of intensive investigation but to date must be classified in the realm of the unsolved.
  • Tetraethyl lead is universally used as an anti-knock agent but other tetraalkyl lead compounds such as tetramethyl lead, tetrabutyl lead, tetraamyl lead, tetrapropyl lead, etc., possess anti-knock properties and may be used in the fuel compositions of the invention.
  • Tetraethyl lead mixtures commercially available for automotive use contain an ethylene chloride-ethylene bromide mixture as a scavenger for removing lead from the combustion chamber in the form of volatile lead halides.
  • Tetraethyl lead fluid denotes the commercial product which comprises tetraethyl lead, ethylene chloride and ethylene bromide, the latter two reagents being present in 1.0 theory and 0.5 theiory, respectively, theory denoting the stoichiometric amount required for reaction with the lead content of the tetraethyl lead.
  • the organo-lead reagent is present in the fuel compositions of the invention in concentrations between 0.5 ml. per gallon up to the statutory limit of organo-lead reagent concentration which, at the present time, is 4 cc. per gallon in the case of automotive fuel and 4.6 ml. per gallon in the case of aviation fuel.
  • the usual concentration of tetraethyl lead is between 1 and 3 cc. per gallon in automotive gasoline and 2 to 4.6 cc. per gallon in aviation gasoline.
  • An octane appreciating action is obtained with acid, t-alkyl esters and aldehydes at concentration of 6 cc. TEL per gallon and higher.
  • TEL per gallon are represented by the general formula: RCOOR' wherein R is hydrogen or a hydrocarbyl radical containing 1-29 and preferably 1 to 7 carbon atoms and R is hydrogen or tertiary aliphatic hydrocarbyl radical of 4-18 and preferably 4 to 12 carbon atoms.
  • the hydrocarbyl monocarboxylic acid can be aliphatic, cycloaliphatic or aromatic in nature.
  • effective monocarboxylic acids are the following: acetic acid, propionic acid, 2-ethylhexanoic acid, stearic acid, curnic acid, benzoic acid, cyclohexane carboxylic acid and phenylacetic acid.
  • the most effective monocarboxylic acids are aliphatic and aryl acids containing between 2 and 8 carbon atoms per molecule; the preferred acids accordingly are acetic acid, propionic acid, benzoic acid, pentanoic acid and Z-ethylhexanoic acid.
  • Tertiary alkyl esters which are the preferred octane appreciators for commercial use because of their ready preparation from available raw materials and their noncorrosive nature, are exemplified by the following: tbutyl acetate, t-butyl propionate, t-amyl propionate, t-amyl acetate, t-butyl benzoate, t-butyl 2-ethylhexanoate, t-octyl acetate and t-dodecylpropionate.
  • the preferred t-alkyl esters are derived from aliphatic and aromatic monocarboxylic acids containing 2-8 carbon atoms and a tertiary aliphatic hydrocarbyl radical containing 4l2 carbon atoms.
  • Aldehydes effective in raising the octane rating of leaded saturated aliphatic hydrocarbon gasoline having an RON of at least 102 when leaded with 3 cc. of TEL per gallon are represented by the formula: RCHO wherein R is a hydrocarbyl radical containing 1-29 and preferably 1 to 7 carbon atoms.
  • R is a hydrocarbyl radical containing 1-29 and preferably 1 to 7 carbon atoms.
  • Preferred aldehydes are those containing 2-8 carbon atoms, i.e. those aldehydes wherein R in the above formula denotes a hydrocarbyl radical containing 1+7 carbon atoms.
  • aldehydes examples include prop ionaldehyde, benzaldehyde, n-butyraldehyde, isobutyraldehyde, acetaldehyde, and paraldehyde, the trimer of acetaldehyde.
  • the octane appreciators must be present in a leaded saturated aliphatic hydrocarbon fuel having a minimum prescribed RON in a concentration of at least 0.1 volume percent before any significant octane appreciation is realized.
  • the most effective concentration of octane appreciator varies with the lead content of the fuel but generally falls in the range between 0.2 and 1.5 volume percent with maximum results normally being obtained between 0.5 and 1.0 volume percent.
  • the upper limit of octane appreciator concentration is placed at 2.0 volume percent both because of economic considerations and because the octane appreciating action of monocarboxylic acids, t-alkyl esters and aldehydes tends to dissappear at about this. concentration level.
  • concentration level The amount of octane appreciation realized with these agents decreases as their concentration exceeds the 1.5 volume percent concentration level.
  • the action of monocarboxylic acids, t-alkyl esters and aldehydes in saturated aliphatic hydrocarbon fuels having a minimum RON of 102 when leaded with 3 cc. of TEL per gallon is shown in Table I.
  • the base fuel employed in Table I is an isobutylene-isobutane alkylate fraction which when leaded with 3 cc. of TEL per gallon had an RON of 106.2 and an MON of 106.0. This base fuel had an olefin plus aromatic content by Flourescent Indicator Analysis (FIA) less than 1 percent.
  • FIA Flourescent Indicator Analysis
  • This base fuel was essentially the same as that employed in Table I above which had an olefin plus aromatic content by Fluorescent Indicator Analysis less than 1% EFFECT OF t-BUTYL ACETATE CONCENTRA- TIONS ABOVE 2 VOLUME PERCENT IN AVIA- TION ALKYLATE CONTAINING 3 CC. OF TEL PER. GALLON AND HAVING AN RON OF 106.8
  • Base Fuel A employed in Table II consisted essentially of 2,4-dimeth ylpentane and had an RON of 97.8 with 3 cc. of TEL per gallon.
  • Base Fuel B was a light straight run naphtha having a boiling point range of 94-207" F. and an RON of 86.8 with 3 cc. of TEL per gallon.
  • Base Fuel C employed in Table III was a blend comprising 90% isobutane-isobutylene alkylate and of n-heptane and had an RON of 98.7 and an MON of 101.9 with 3 cc. of TEL per gallon.
  • FIA indicated that this fuel had an aromatic plus olefin content less than 1%.
  • Base Fuel D employed in Table HI comprised 84% isobutane-isobutylene alkylate and 16% n-heptane and had an RON of 98.0 and an MON of 101.4 with 3 cc. TEL per gallon. FIA analysis indicated that this fuel had an aromatic plus olefin content less than 1%.
  • Base Fuel E was a blend comprising 91% isobutaneisobutylene alkylate and 9% Udex raflinate and had an RON of 102 and an MON of 103.3 with 3 cc. TEL per gallon. FIA showed that the aromatic plus olefin content of this fuel was less than 1 volume percent. Udex raffinate is a residual fraction obtained in diethylene glycol extraction of catalytic reformate.
  • Base Fuel F is a blend of 95% isobutane-isobutylene alkylate and 5% Udex rafiinate and had an RON of 103.5 and an MON of 106.0 with 3 cc. of TEL per gallon. FLA indicated that the aromatic plus olefin content of this fuel was less than 1 volume percent.
  • Table V show the octane appreciating action of acids and t-alkyl esters on the RON of a leaded paraflinic reference fuel comprising 10% isopentane, 5% nheptane and isooctane and having an RON of 104.9 and an MON of 110.3 with 3 cc. of TEL per gallon.
  • a hydrocarbon fuel in the gasoline boiling range consisting essentially of saturated aliphatic hydrocarbons having a minimum research octane number with 3 cc. of tetraethyl lead per .gallon of 102, said fuel containing an organo-lead antidcnock agent in a concentration of at least 0.5 cc. per gallon and 0.1 to 2.0 volumepercent of an oxygenated hydrocarbon selected from the group consisting of t-alkyl esters of a hydrocarbyl monocarboxylic acid, said monocarboxylic acids containing from 1- to 30 carbon atoms, said concentration of said oxygenated hydrocarbons effecting a substantial improvement in the research octane number of said saturated aliphatic hydrocarbon fuel.
  • RCOOR' in which R is selected from the group consisting of hydrogen and hydrocarbyl radicals containing 1 to 29 carbon atoms and R is selected from the group consisting of a tertiary aliphatic hydrocarbon radical containing 4 to 18 carbon atoms.
  • a hydrocarbon fuel in the gasoline boiling range consisting essentially of saturated aliphatic hydrocarbons having a minimum RON with 3 cc. of tetraethyl lead per gallon of 102, said fuel containing an alkyllead anti-knock agent in a concentration of at least 0.5 cc. per gallon and 0.1 to 2.0 volume percent of an oxygenated hydrocarbon selected from the group consisting of oxygenated hydrocarbons of the general formula:
  • RCOOR' wherein R is a hydrocarbon radical containing 1 to 7 carbon atoms per molecule and R is a tertiary aliphatic hydrocarbon radical containing 4 to 12 carbon atoms, said concentration of said oxygenated hydrocarbon effecting a substantial improvement in the research octane number of said saturated aliphatic hydrocarbon fuel.
  • a hydrocarbon fuel according to claim 5 containing 1.0 to 4.6 cc. of tetraethyl lead per gallon.

Description

United States Patent Office 3,421,867 SATURATED ALIPHATIC HYDROCARBON GASOLINE Robert Y. lleisler and Kenneth L. Dille, Wapplngers Falls, N.Y., Marc F. Fontaine, Houston, Ten and George W. Eclrert, Wagpingers Falls, N.Y., asslgnors to Texaco Inc., New ork, N.Y., a corporation of Delaware No Drawing. Continuation of application Ser. No.
350,650, Mar. 10, 1964. This application Mar. 3, 1966, Ser. No. 531,350
US. Cl. 44-66 9 Claims Int. Cl. Cll 1/14 This application is a continuation of application S.N.
350.650 now abandoned filed on Mar. 10, 1964. This invention relates to hydrocarbon fuel compositions of high octane rating. More specifically, it involves the discovery that the octane rating of leaded saturated aliphatic fuels having .a minimum Research Octane Number is substantiallly improved by the addition of prescribed concentrations of an oxygentated hydrocarbon compound.
Patented Jan. 14, 1969 filed Dec. 23, i957 it is disclosed that hydrocarbyl aldehydes in similar concentrations are effective octane appreciators in leaded fuels having a minimum aromatic boxylic acids, t-alkyl esters thereof and aldehydes are The recent increases in compression ratios of automobile engines have placed a severe strain on petroleum refiners to produce fuels having the octane ratinfg demanded by these engines. Premium fuels at the present time have Research Octane Ratings between 97 and 100 and it has ben predicted that premium fuels will have to have octane ratings betwen and five years from now in order to satisfy the octane requirements of the high compression automotive engines predicted for that date. In order to produce premium fuels of octane ratings of 95 and above, it has been necessary for refiners to rely heavily on catalytic refining operations such as fluid catalytic cracking, catalytic reforming, alkylation and catalytic isomerization.
Catalytic cracking and catalytic reforming, which are the most widely used refining operations in the production of high octane fuels, produce substantial quantities of aromatics; catalytic crac ting also produces a substantial amount of olefins. It i well known that olefinsand aromatics, although possessing high octane ratings, have a poorer response to organo-lead compounds such as tetraethyl lead than saturated aliphatic gasoline components. Accordingly, as the aromatic and olefinic content of the gasolines have increased to meet the octane levels required by modern automotive high compression engines, the lead response of the resulting fuels has diminished. Stated another way, the cctane increment obtained by the addition of an organo-lead compound decreases as the aromatic and olefin cot'ttents of the base fuel increase.
The subject invention is a C-I-P of application S.N. 847,086 filed on Oct. 19, 1959. which is an extension of the discovery that hydrocarbyl monocarboxylic acids, certain derivatives and precursors therof have an octane appreciating action in leaded fuels having a minimum concentration of aromatics and/or olefin hydrocarbons.
In the commonly-assigned copending application Ser. No.
689.466 filed Oct. ll, 1957, by G. W. Eckert, it is disclosed that hydrocarbyl monocarboxylic acids in concentrations of the order of 0.1 to 5.0 volume percent and preferably between 0.2 and 2.0 volume percent, act as octane appreciators in leaded fuels having a minimum aromatic and/or olefinic content of the order of 10 percent. ln commonly assigned copending applications Ser. No. 699.944 filed Dec. 2, i957 and its C-l-P, Ser No. 743,001 filed June I9, 1958 in the names of G. W. Eckert, and H. V. Hess and E. C. Knowles, it is disclosed that t-alkyl esters of hydrocarbyl monocarhoxylic acids in similar concentrations act as octane appreciators in leaded fuels having a minimum aromatic and/or olefinic concentration of the order of 5 percent. In another commonly-assigned copending application Ser. No. 704,303
effective octane appreciators in leaded fuels consisting essentially of saturated aliphatic hydrocarbons provided the mixture of leaded saturated paraffinic hydrocarbons has a minimum Research Octane Number (RON).
The high octane hydrocarbon motor fuel of this invention consists essentially of saturated aliphatic hydro carbons, an organo'lead anti-knock agent, said saturated aliphatic hydrocarbons having a-minimum RON with i 3 cc. of tetraethyl lead (TEL) per gallon of 102, and
0.l2.0 volume percent of an oxygenated hydrocarbon which is either a hydrocarbyl monocarboxylic acid containing 1-30 carbon atoms, a t-alkyl ester of said hydrocarbyl monocarboxylic acid, or a hydrocarbyl aldehyde containing 2-30 carbon atoms. When employed in the prescribed concentration and particularly when employed in concentrations between 0.2 and 1.5 volume percent,
hydrocarbyl monocarboxylic acids, t-alkyl esters thereof and hydrocarbyl aldehydes substantially improve the carbon fuel having the prescribed minimum RON with 3 cc. of tetraethyl lead per gallon of 102.
Similarly to their octane appreciating action in leaded fuels of minimum aromatic and/or olefinic content which forms the subject matter of the previously-identified copending applications, monocarboxylic acids, t-alkyl' esters and aldehydes are ineffective in raising the octa'ne. rating of a saturated aliphatic hydrocarbon fuel of minimum RON in the absence of the organo-lead anti-knock agent which is normally TEL. The presence of lead is a requisite for the octane appreciating action of these agents, which fact definitely proves'that these agents in raising the octane rating of the saturated paraffinic fuel 'of minimum octane number are not acting as blending agents. As a matter of fact, the presence of these agents in unleaded fuels in the concentrations above those prescribed herein actually slightly degrades the octane rating of a clear, i.e. unleaded saturated aliphatic hydrocarbon fuel such as alkylate.
A second unusual characteristics of the action of monocarboxylic acids, t-alkyl esters thereof and aldehydes in having an RON rating with 3 cc. of lead per gallon below the prescribed minimum of 102. The reason for the ineffectiveness of these agents in saturated parafiinic fuels of octane rating below the prescribed minimum and their effectiveness in such fuels above the prescribed octane level is currently the subject of intensive investigation but to date must be classified in the realm of the unsolved.
Another unusual feature of the octane appreciating action of monocarboxylic acids, t-alkyl esters and aldehydes in saturated aliphatic hydrocarbon fuels of minimum RON is the fact that the octane appreciating action is apparently restricted to the Research Octane No. These agents do not raise the Motor Octane No. of saturated aliphatic hydrocarbon fuels having Research Octane The organo-lead reagent necessary for the action of monocarboxylic acids, t-alkyl esters and aldehydes as octane improvers is a tetraalkyl lead compound of the class known to possess anti-knock action. Tetraethyl lead is universally used as an anti-knock agent but other tetraalkyl lead compounds such as tetramethyl lead, tetrabutyl lead, tetraamyl lead, tetrapropyl lead, etc., possess anti-knock properties and may be used in the fuel compositions of the invention.
The tetraethyl lead mixtures commercially available for automotive use contain an ethylene chloride-ethylene bromide mixture as a scavenger for removing lead from the combustion chamber in the form of volatile lead halides. Tetraethyl lead fluid denotes the commercial product which comprises tetraethyl lead, ethylene chloride and ethylene bromide, the latter two reagents being present in 1.0 theory and 0.5 theiory, respectively, theory denoting the stoichiometric amount required for reaction with the lead content of the tetraethyl lead.
The organo-lead reagent is present in the fuel compositions of the invention in concentrations between 0.5 ml. per gallon up to the statutory limit of organo-lead reagent concentration which, at the present time, is 4 cc. per gallon in the case of automotive fuel and 4.6 ml. per gallon in the case of aviation fuel. The usual concentration of tetraethyl lead is between 1 and 3 cc. per gallon in automotive gasoline and 2 to 4.6 cc. per gallon in aviation gasoline. An octane appreciating action is obtained with acid, t-alkyl esters and aldehydes at concentration of 6 cc. TEL per gallon and higher.
The hydrocarbyl monocarboxylic acids and their t-alkyl esters effective in raising the octane rating of leaded saturated gasoline hydrocarbons having a minimum RON of 102 with 3 cc. TEL per gallon are represented by the general formula: RCOOR' wherein R is hydrogen or a hydrocarbyl radical containing 1-29 and preferably 1 to 7 carbon atoms and R is hydrogen or tertiary aliphatic hydrocarbyl radical of 4-18 and preferably 4 to 12 carbon atoms.
The hydrocarbyl monocarboxylic acid can be aliphatic, cycloaliphatic or aromatic in nature. Examples of effective monocarboxylic acids are the following: acetic acid, propionic acid, 2-ethylhexanoic acid, stearic acid, curnic acid, benzoic acid, cyclohexane carboxylic acid and phenylacetic acid. In general, the most effective monocarboxylic acids are aliphatic and aryl acids containing between 2 and 8 carbon atoms per molecule; the preferred acids accordingly are acetic acid, propionic acid, benzoic acid, pentanoic acid and Z-ethylhexanoic acid.
Tertiary alkyl esters, which are the preferred octane appreciators for commercial use because of their ready preparation from available raw materials and their noncorrosive nature, are exemplified by the following: tbutyl acetate, t-butyl propionate, t-amyl propionate, t-amyl acetate, t-butyl benzoate, t-butyl 2-ethylhexanoate, t-octyl acetate and t-dodecylpropionate. The preferred t-alkyl esters are derived from aliphatic and aromatic monocarboxylic acids containing 2-8 carbon atoms and a tertiary aliphatic hydrocarbyl radical containing 4l2 carbon atoms.
Aldehydes effective in raising the octane rating of leaded saturated aliphatic hydrocarbon gasoline having an RON of at least 102 when leaded with 3 cc. of TEL per gallon are represented by the formula: RCHO wherein R is a hydrocarbyl radical containing 1-29 and preferably 1 to 7 carbon atoms. Preferred aldehydes are those containing 2-8 carbon atoms, i.e. those aldehydes wherein R in the above formula denotes a hydrocarbyl radical containing 1+7 carbon atoms. Examples of effective aldehydes are the following: prop ionaldehyde, benzaldehyde, n-butyraldehyde, isobutyraldehyde, acetaldehyde, and paraldehyde, the trimer of acetaldehyde.
The octane appreciators must be present in a leaded saturated aliphatic hydrocarbon fuel having a minimum prescribed RON in a concentration of at least 0.1 volume percent before any significant octane appreciation is realized. The most effective concentration of octane appreciator varies with the lead content of the fuel but generally falls in the range between 0.2 and 1.5 volume percent with maximum results normally being obtained between 0.5 and 1.0 volume percent. The upper limit of octane appreciator concentration is placed at 2.0 volume percent both because of economic considerations and because the octane appreciating action of monocarboxylic acids, t-alkyl esters and aldehydes tends to dissappear at about this. concentration level. The amount of octane appreciation realized with these agents decreases as their concentration exceeds the 1.5 volume percent concentration level.
The action of monocarboxylic acids, t-alkyl esters and aldehydes in saturated aliphatic hydrocarbon fuels having a minimum RON of 102 when leaded with 3 cc. of TEL per gallon is shown in Table I. The base fuel employed in Table I is an isobutylene-isobutane alkylate fraction which when leaded with 3 cc. of TEL per gallon had an RON of 106.2 and an MON of 106.0. This base fuel had an olefin plus aromatic content by Flourescent Indicator Analysis (FIA) less than 1 percent.
TABLE I.IMPROVEMENI IN RON AND MON 0F LEADED ALKYLATE 106+ RON LEVEL The data in the above table indicate that monocarboxylic acids, t-alkyl esters and aldehydes have a significant octane appreciating action on the RON of saturated aliphatic hydrocarbon fuels having the prescribed minimum leaded RON. It is significant that the same improvement was not noted in the MON of the leaded alkylate fuel on addition of t-butyl acetate. This phenomenon, that is, the increase in RON without a corresponding increase in MON is unique with saturated aliphatic hydrocarbon gasolines. These agents effect substantially equivalent increases in the RON and MON ratings of leaded gasoline containing an aromatic and/or olefin content above 5 volume percent.
The critical nature of the upper concentration limit of 2.0 volume percent for the action of tertiary alkyl esters in improving the Research Octane Number of a leaded gasoline consisting essentially of saturated aliphatic hydrocarbons and having a minimum RON of 102 with 3 cc. of TEL per gallon is established by the data in the following table showing that 3, 4 and 5 volume percent of t-butyl acetate in leaded aviation alkylate actually decreased the Research Octane Number of the base fuel. The base fuel employed in obtaining this data was an isobutane-butylene alkylate fraction containing 3 cc. of TEL per gallon and having an RON of 106.8. This base fuel was essentially the same as that employed in Table I above which had an olefin plus aromatic content by Fluorescent Indicator Analysis less than 1% EFFECT OF t-BUTYL ACETATE CONCENTRA- TIONS ABOVE 2 VOLUME PERCENT IN AVIA- TION ALKYLATE CONTAINING 3 CC. OF TEL PER. GALLON AND HAVING AN RON OF 106.8
Percent of t-butyl acetate in base fuel: Change in RON 3 -2.8 4 -3.9 5 -4.0
In Table II there is demonstrated the ineffectiveness of monocarboxylic acid, t-alkyl esters thereof and aldehydes in raising the octane rating of saturated aliphatic hydrocarbon fuels having an RON below the minimum of 102 when containing 3 cc. of TEL per gallon. Base Fuel A employed in Table II consisted essentially of 2,4-dimeth ylpentane and had an RON of 97.8 with 3 cc. of TEL per gallon. Base Fuel B was a light straight run naphtha having a boiling point range of 94-207" F. and an RON of 86.8 with 3 cc. of TEL per gallon.
The data in Table II show the ineffectiveness of hydrocarbyl monocarboxylic acids in raising the octane rating of saturated aliphatic hydrocarbon fuels whose RON with 3 cc. of TEL per gallon is less than 102. Although data on MON is not shown, there was no increase in MON by the addition. of the octane appreciators to saturated aliphatic hydrocarbon fuels of the type shown above.
In Table III there are presented data demonstrating the fact that an RON with 3 cc. of TEL per gallon of 102 is the critical minimum required for monocarboxylic acids, t-alkyl esters thereof and aldehydes to act as octane appreciators in leaded saturated aliphatic hydrocarbon fuels. The data presented in Table III show clearly that an -RON with 3 cc. TEL per gallon of 102 provides a line of demarcation between the effectiveness and ineffectiveness of the prescribed octane appreciators in improving the RON of saturated aliphatic hydrocarbon fuels.
Base Fuel C employed in Table III was a blend comprising 90% isobutane-isobutylene alkylate and of n-heptane and had an RON of 98.7 and an MON of 101.9 with 3 cc. of TEL per gallon. FIA indicated that this fuel had an aromatic plus olefin content less than 1%.
Base Fuel D employed in Table HI comprised 84% isobutane-isobutylene alkylate and 16% n-heptane and had an RON of 98.0 and an MON of 101.4 with 3 cc. TEL per gallon. FIA analysis indicated that this fuel had an aromatic plus olefin content less than 1%.
Base Fuel E was a blend comprising 91% isobutaneisobutylene alkylate and 9% Udex raflinate and had an RON of 102 and an MON of 103.3 with 3 cc. TEL per gallon. FIA showed that the aromatic plus olefin content of this fuel was less than 1 volume percent. Udex raffinate is a residual fraction obtained in diethylene glycol extraction of catalytic reformate.
Base Fuel F is a blend of 95% isobutane-isobutylene alkylate and 5% Udex rafiinate and had an RON of 103.5 and an MON of 106.0 with 3 cc. of TEL per gallon. FLA indicated that the aromatic plus olefin content of this fuel was less than 1 volume percent.
The results of adding 0.75% of t-butyl acetate to these various base fuels is shown in Table III.
TABLE III.EFFECT 0F t-BUTYL ACETATE ON THE RON AND MON OF SATURATED ALIPHATIC HYDROCARBON FUELS Increase RON MON Base fuel 0 (RON 98.6)+0.75 v. percent t-butyl acetate 0.1 -O.1 Base Iuel D (RON 98.0)+0.75 v. percent t-butyl acetate 0.0 0.0 Base fuel E (RON 102.0)+0.75 v. percent t-butyl acetate +0.2 0.3 Base fuel F (RON 103.5)+0.75 v. percent t-butyl acetate. +0.2 0.4
effective in saturated aliphatic hydrocarbon fuels as the octane level rises. This is shown in Table IV demonstrating the action of t-butyl acetate in a concentration of 0.75 volume percent in an isobutane-isobutylene alkylate fraction having an RON of 108.7 and an MON of 107.6 with 3 cc. of TEL per gallon.
TABLE IV.ACTION OF t-BUTYL ACETATE IN AN ALKYLATE HAVING 108.7 RON WITH 3 CC. TEL PER GALLON Base Fuel+0.75 v. percent t-butyl acetate (increase):
RON 1.6
MON 0.0
A comparison of the 1.6 RON improvement obtained by the presence of 0.75 volume percent t-butyl acetate in the 108.7 RON leaded alkylate in the above table with the 0.7 unit improvement obtained with the same concentration of t-butyl acetate in the 106.2 RON leaded alkylate of Table I shows the increasing effectiveness of the octane appreciators in saturated aliphatic hydrocarbon fuels as the RON of the base fuel exceeds the minimum level of 102.
The data in Table V show the octane appreciating action of acids and t-alkyl esters on the RON of a leaded paraflinic reference fuel comprising 10% isopentane, 5% nheptane and isooctane and having an RON of 104.9 and an MON of 110.3 with 3 cc. of TEL per gallon.
TABLE V.ACTION OF ACIDS AND t-ALKYL ESTERS IN SATURATED ALIPHATIC HYDRO- CARBON REFERENCE FUEL CONTAINING 3 CC. TEL PER GALLON Increase in RON Reference Fuel+0.5% benzoic acid 0.4 Reference Fuel+1.0% benzoic acid 0.5- Reference Fuel+0.75% t-butyl acetate +0.3 Reference Fuel+0.75% t-butyl propionate +0.3
Obviously, many modifications and variations of the invention as hereinbefore set forth may be made Without departing from the spirit and scope thereof and, therefore, only such limitations should be imposed as are indicated in the appended claims.
We claim:
1. A hydrocarbon fuel in the gasoline boiling range consisting essentially of saturated aliphatic hydrocarbons having a minimum research octane number with 3 cc. of tetraethyl lead per .gallon of 102, said fuel containing an organo-lead antidcnock agent in a concentration of at least 0.5 cc. per gallon and 0.1 to 2.0 volumepercent of an oxygenated hydrocarbon selected from the group consisting of t-alkyl esters of a hydrocarbyl monocarboxylic acid, said monocarboxylic acids containing from 1- to 30 carbon atoms, said concentration of said oxygenated hydrocarbons effecting a substantial improvement in the research octane number of said saturated aliphatic hydrocarbon fuel.
2. A hydrocarbon fuel according to claim 1 in which said oxygenated hydrocarbon is present in a concentration between 0.2 and 1.5 volume percent.
3. A hydrocarbon fuel according to claim 1 in which said organo-lead, anti-knock agent is present in a concentration between 0.5 and 4.6 cc. per gallon.
4. A hydrocarbon fuel according to claim 1 in which said esters have the general formula:
RCOOR' in which R is selected from the group consisting of hydrogen and hydrocarbyl radicals containing 1 to 29 carbon atoms and R is selected from the group consisting of a tertiary aliphatic hydrocarbon radical containing 4 to 18 carbon atoms.
5. A hydrocarbon fuel in the gasoline boiling range consisting essentially of saturated aliphatic hydrocarbons having a minimum RON with 3 cc. of tetraethyl lead per gallon of 102, said fuel containing an alkyllead anti-knock agent in a concentration of at least 0.5 cc. per gallon and 0.1 to 2.0 volume percent of an oxygenated hydrocarbon selected from the group consisting of oxygenated hydrocarbons of the general formula:
RCOOR' wherein R is a hydrocarbon radical containing 1 to 7 carbon atoms per molecule and R is a tertiary aliphatic hydrocarbon radical containing 4 to 12 carbon atoms, said concentration of said oxygenated hydrocarbon effecting a substantial improvement in the research octane number of said saturated aliphatic hydrocarbon fuel.
6. A hydrocarbon fuel according to claim 5 in which the concentration of oxygenated hydrocarbon is between 0.2 and 1.5 volume percent.
7. A hydrocarbon fuel according to claim 5 containing 1.0 to 4.6 cc. of tetraethyl lead per gallon.
3. A hydrocarbon fuel according to claim 5 in which said oxygenated hydrocarbon is t-butyl acetate.
9. A hydrocarbon fuel according to claim 5 in which said oxygenated hydrocarbon is t-butyl propionate.
References Cited UNITED STATES PATENTS 1,692,784 1l/l928 Orelup et a1. 44-68 2,210,942 8/1940 Lipkin 4477 2,228,662 l/194l Holm 4470 2,360,585 10/1944 Ross et a1 44-80 FOREIGN PATENTS 202,264 12/1922 Great Britain.
277,326 l/l929 Great Britain.
837,965 11/1938 France.
640,311 3/1928 France.
OTHER REFERENCES Improved Motor Fuels Through Selective Blending," Wagner et al., paper presented before the American Pctroleum Institute, Nov. 7, 1941, FIGS. 8-13.
DANIEL F. WYMAN, Primary Examiner.
Y. H. SMITH, Assistant Examiner.
US. Cl. X.R. 4469,

Claims (1)

1. A HYDORCARBON FUEL IN THE GASOLINE BOILING RANGE CONSISTING ESSENTIALLY OF SATURATED ALIPHATIC HYDROCARBONS HAVING A MINIMUM RESEARCH OCTANE NUMBER WITH 3CC. OF TETRAETHYL LEAD PER GALLON OF 102, SAID FUEL CONTAINING AN ORGANO-LEAD ANTI-KNOCK AGENT IN A CONCENTRATION OF AT LEAST 0.5 CC. PER GALLON AND 0.1 TO 2.0 VOLUME PERCENT OF AN OXYGENATED HYDROCARBON SELECTED FROM THE GROUP CONSISTING OF T-ALKYL ESTERS OF A HYDROCARBYL MONOCARBOXYLIC ACID, SAID MONOCARBOXYLIC ACIDS CONTAINING FROM 1 TO 30 CARBON ATOMS, SAID CONCENTRATION OF SAID OXYGENATED HYDROCARBONS EFFECTING A SUBSTANTIAL IMPROVEMENT IN THE RESEARCH OCTANE NUMBER OF SAID SATURATED ALIPHATIC HYDROCARBON FUEL.
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4444565A (en) * 1982-12-20 1984-04-24 Union Oil Company Of California Method and fuel composition for control of octane requirement increase
US4612880A (en) * 1982-12-20 1986-09-23 Union Oil Company Of California Method for control of octane requirement increase in an internal combustion engine having manifold and/or combustion surfaces which inhibit the formation of engine deposits
US4737159A (en) * 1984-06-29 1988-04-12 E. I. Du Pont De Nemours And Company Corrosion inhibitor for liquid fuels
WO2010000761A1 (en) * 2008-07-02 2010-01-07 Shell Internationale Research Maatschappij B.V. Liquid fuel compositions
US20100000483A1 (en) * 2008-07-02 2010-01-07 Lionel Clarke Gasoline compositions
US20110000124A1 (en) * 2009-07-01 2011-01-06 Jurgen Johannes Jacobus Louis Gasoline compositions

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GB202264A (en) * 1922-08-12 1924-06-05 Henri Terrisse Process for the preparation of a carburetting fuel mixture for internal combustion engines
FR640311A (en) * 1926-09-07 1928-07-10 Avenarius Soc Geb Method and means for preventing knocking caused by motor fuels
US1692784A (en) * 1925-01-23 1928-11-20 Boyce Ite Products Inc Fuel and fuel ingredients
GB277326A (en) * 1927-09-06 1929-01-07 Avenarius Geb A method for preventing the knocking of motor fuel
FR837965A (en) * 1937-11-08 1939-02-23 Melle Usines Sa Detonation resistant fuels
US2210942A (en) * 1936-10-20 1940-08-13 Atlantic Refining Co Motor fuel
US2228662A (en) * 1939-05-31 1941-01-14 Standard Oil Co Motor fuel
US2360585A (en) * 1941-10-27 1944-10-17 Pure Oil Co Motor fuel

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB202264A (en) * 1922-08-12 1924-06-05 Henri Terrisse Process for the preparation of a carburetting fuel mixture for internal combustion engines
US1692784A (en) * 1925-01-23 1928-11-20 Boyce Ite Products Inc Fuel and fuel ingredients
FR640311A (en) * 1926-09-07 1928-07-10 Avenarius Soc Geb Method and means for preventing knocking caused by motor fuels
GB277326A (en) * 1927-09-06 1929-01-07 Avenarius Geb A method for preventing the knocking of motor fuel
US2210942A (en) * 1936-10-20 1940-08-13 Atlantic Refining Co Motor fuel
FR837965A (en) * 1937-11-08 1939-02-23 Melle Usines Sa Detonation resistant fuels
US2228662A (en) * 1939-05-31 1941-01-14 Standard Oil Co Motor fuel
US2360585A (en) * 1941-10-27 1944-10-17 Pure Oil Co Motor fuel

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4444565A (en) * 1982-12-20 1984-04-24 Union Oil Company Of California Method and fuel composition for control of octane requirement increase
US4612880A (en) * 1982-12-20 1986-09-23 Union Oil Company Of California Method for control of octane requirement increase in an internal combustion engine having manifold and/or combustion surfaces which inhibit the formation of engine deposits
US4737159A (en) * 1984-06-29 1988-04-12 E. I. Du Pont De Nemours And Company Corrosion inhibitor for liquid fuels
WO2010000761A1 (en) * 2008-07-02 2010-01-07 Shell Internationale Research Maatschappij B.V. Liquid fuel compositions
US20100000484A1 (en) * 2008-07-02 2010-01-07 Alison Felix-Moore Liquid fuel compositions
US20100000483A1 (en) * 2008-07-02 2010-01-07 Lionel Clarke Gasoline compositions
US20110000124A1 (en) * 2009-07-01 2011-01-06 Jurgen Johannes Jacobus Louis Gasoline compositions

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