US3238026A - Fuel oils - Google Patents

Fuel oils Download PDF

Info

Publication number
US3238026A
US3238026A US226741A US22674162A US3238026A US 3238026 A US3238026 A US 3238026A US 226741 A US226741 A US 226741A US 22674162 A US22674162 A US 22674162A US 3238026 A US3238026 A US 3238026A
Authority
US
United States
Prior art keywords
oil
additive
gelation
copper
oils
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
US226741A
Inventor
Noel Fernand
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.)
ExxonMobil Technology and Engineering Co
Original Assignee
Exxon Research and Engineering 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 Exxon Research and Engineering Co filed Critical Exxon Research and Engineering Co
Priority to US226741A priority Critical patent/US3238026A/en
Application granted granted Critical
Publication of US3238026A publication Critical patent/US3238026A/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
    • C10L1/2425Thiocarbonic acids and derivatives thereof, e.g. xanthates; Thiocarbamic acids or derivatives thereof, e.g. dithio-carbamates; Thiurams

Definitions

  • the present invention is concerned with improving the characteristics of fuel oils, particularly furnace fuel oils and the like. More particularly, the present invention relates to the preparation of fuel oils having improved characteristics with respect to undesirable mercaptide gel formation and having improved anti-oxidant properties. In particular, the present invention relates to heating oils and diesel fuels, kerosenes, aviation turbojet fuels, and other fuels that are subject to mercaptide gel formation.
  • middle distillates are naturally improved with respect to mercaptide .gel formation and anti-oxidant properties by incorporating therein an effective amount of t-alkylamrnonium talkyldithiocarbamate.
  • the compound is one which is characterized by having the alkyl group highly branched and cotnaining from about 8 to 30, preferably 12 to 22, carbon atoms in the alkyl groups. It is therefore the principal object of the present invention to set forth a mercaptide gelation inhibitor for middle distillates and lighter fuels. In general, these oil boil in the range from 250 to about 750 F. It is a still further object of the present invention to provide heating oils, diesel fuel oils, kerosene and jet fuels with improved antioxidant properties.
  • furnace fuels particularly those containing small amounts of mercaptans
  • this gelation is due to a reaction between the mercaptans in the oil and copper from the brass fittings which leads to the formation of oil insoluble copper mercaptides.
  • Copper mercaptides derived from long chain aliphatic mercaptans, e.g. n-dodecanethiol have an ability to effect gelation of the oil medium.
  • the resulting gel is commonly called mercaptide gel.
  • the present invention by the use of t-alkylammonium t-alkyldithiocarbamates, prevents the mercaptide gel formation as well as precipitation of the copper mercaptide.
  • Fuel oils particularly non-hydrofined furnace fuel oils, also have a tendency to form color and sediment when stored exposed to the air.
  • the formation of sediment is particularly undesirable since it eventually effects plugging of line filters and fine orifices, such as burner nozzles and fuel injectors.
  • the present invention by use of t-alkylamrnonium t-alkyldithiocarbamates, will inhibit sediment formation in the fuel oils being stored.
  • the particular t-alkylamrnonium t-alkyldithiocarbamates of the present invention can be synthesized by slowly adding one mole of carbon disulfide to two moles of a tertiary alkyl primary amine, in which the alkyl group is highly branched.
  • the number of carbon atoms in the alkyl group of the primary amine ranges from about 8 to 30 but the preferred range is from about 12 to 22.
  • the reaction temperature is maintained in the range from about 25 C. to 35 C., preferably at a temperature of about 30 C. The following reaction occurs:
  • t-alkylammonium t-alkyldithiocarbamates used may vary depending upon the particular base oil as, for example, in the range from about 0.0001 to 05 wt. percent, preferably in the range from about 0.005 to 0.1 wt. percent based on the oil.
  • t-alkylammonium t-alkyldithiocarbamates be of the following type:
  • R is any alkyl group which must be branched.
  • a few typical members of this class of compounds are: l,l,3,3-tetramethyl butylammonium, 1,1,3,3-tetramethylbutyldithiocarbamate, and 1,l,3,3,5,5 hexamethylhexylammonium l,1,3,3,5,5-hexamethylhexyldithiocarbamate.
  • the alkyl groups of the amines used in the synthesis of the additive can be obtained through olefin polymerization using BF
  • the resulting olefin is a complex mixture, which is rather undefinable as olefin tetramers. Consequently, the conversion of these olefin polymers to amines will also afford rather undefinable amine mixtures. Nevertheless, these amines, because of their branchiness, hence increased oil solubility, are preferably used for the synthesis of t-alkylammonium t-alkyldithiocarbamates.
  • Such amines are commercially available and are commonly referred to as Prirnene 8l-R and Primene J.M.T.
  • t-alkylammonium t-alkyldithiocarbamates of the present invention should have molecular weights ranging from about 334 to about 950 but preferably from about 446 to about 726.
  • Typical distillate fuels boiling in the range from 250 to 750 F. to which the present additives may be added are middle distillate heating oils. These fuels are of commercial grade and have typical properties as follows.
  • EXAMPLE 1 Suitable concentrations of oil soluble copper compounds; that is, cupric naphthenate and an aliphatic mercaptan, i.e. n-dodecanethiol, when added to fuel oils will effect a gelation of the oil.
  • the elfect of the talkyldithiocarbamate on this gelation is shown in the following table. In each of these tests a copper naphthenate solution was added to a solution of the mercaptan and talkyl-ammonium t-alkyldithiocarbamate mixture.
  • Additive added mole/ liter Remarks Nil Rapid gelation of the oil with slight precipitation after 16 hours.
  • EXAMPLE 2 An accelerated test was devised to simulate field conditions to demonstrate the effect of the additive on mercapticle gel formation on an actual copper surface.
  • Copper strips (7X 1.0 cm.) were specially corroded by first polishing with emery cloth, then storing for 24 hours in an ammonia saturated benzene solution.
  • the saturated solution was prepared by shaking benzene with concentrated ammonia solution then separating the henzene layer.
  • the corroded copper strips were then gently wiped, washed in pertoleum ether and air dried before weighing. These copper strips were then suspended in one liter 1:1 blends of lye washed cat. cracked and straight run gas oils. The tests ran at 10 C. for eight hours then room temperature for two days.
  • Composition I Fuel oil blend originally containing 8.4 mg. of mercaptan sulphur per 100 ml. of oil.
  • EXAMPLE 3 Two 121 blends of lye washed cat. cracked gas oil and straight run gas oil were aerated at 20 C. at the rate of 100 cc./minute. To one oil, 0.01% of t-alkylammonium t-alkyldithiocarbamate was added. The dithiocarbamate used here was made by the reaction of carbon disulphide with a mixture of C C t-alkyl primary amines, by the aforementioned synthesis procedure. During the aerations, the ASTM colors of the solutions were determined. The results are given below:
  • EXAMPLE 4 The additive used in these tests was the same as that used in the tests of Example 3. Two oil blends were prepared. Blend A was 4:1 mixture of cat. cracked gas oil and straight run gas oil while Blend B was a 1:1 mixture of the two oils. Each oil used in making the blends had been previously lye washed. Various concentrations of additive were added to the blends, then the resulting solutions were stored in the dark for six weeks in wide mouth open bottles at 43 C. The experimental results are given in Table IV.
  • the amount of sediment was determined in each case by filtration through a fine sintered glass filtering crucible, washing the collected sediment with n-heptane, then drying at C. and weighing when dried.
  • the present invention is concerned with reducing the mercaptide gel formation of hydrocarbon compositions, particularly fuel oil compositions.
  • the invention is particularly applicable to those hydrocarbon compositions having mercaptan numbers above about 10, particularly in the range of from about 10 to 100.
  • the invention is also effective in reducing the tendency for gel formation even on oils having mercaptan numbers in the range from about 4 to 10. It is preferred that the additive concentration approach the concentration of the copper concentration, as for example that the additive concentration be above 50% of the copper concentration.
  • a hydrocarbon fuel oil composition consisting essentially of a major quantity of a hydrocarbon fuel oil containing mercaptans and from 0.0001 to 0.5% by weight based upon the total composition of a t-alkylammonium t-alkyldithiocarbamate having a structural formula as References Cited by the Examiner UNITED STATES PATENTS 2,251,686 8/1941 Musselman et a1. 252402 2,343,393 3/1944 Bergen 252-402 2,912,314 11/1959 Geller et a1. 4472 DANIEL E. WYMAN, Primary Examiner.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

United States Patent Office 3,238,026 Patented Mar. 1, 1966 3,238,026 FUEL OILS Femand Noel, Sarnia, Ontario, Canada, assignor to Essa Research and Engineering Company, a corporation of Delaware No Drawing. Filed Sept. 27, 1962, Ser. No. 226,741 4 Claims. (Cl. 4472) The present invention is concerned with improving the characteristics of fuel oils, particularly furnace fuel oils and the like. More particularly, the present invention relates to the preparation of fuel oils having improved characteristics with respect to undesirable mercaptide gel formation and having improved anti-oxidant properties. In particular, the present invention relates to heating oils and diesel fuels, kerosenes, aviation turbojet fuels, and other fuels that are subject to mercaptide gel formation.
'In accordance with the present invention, middle distillates are naturally improved with respect to mercaptide .gel formation and anti-oxidant properties by incorporating therein an effective amount of t-alkylamrnonium talkyldithiocarbamate. The compound is one which is characterized by having the alkyl group highly branched and cotnaining from about 8 to 30, preferably 12 to 22, carbon atoms in the alkyl groups. It is therefore the principal object of the present invention to set forth a mercaptide gelation inhibitor for middle distillates and lighter fuels. In general, these oil boil in the range from 250 to about 750 F. It is a still further object of the present invention to provide heating oils, diesel fuel oils, kerosene and jet fuels with improved antioxidant properties.
Thus, as pointed out heretofore, furnace fuels, particularly those containing small amounts of mercaptans, have a tendency to produce gels which clog various brass fittings through which the oil normally flows as, for example, in the circuit of a heating oil burner. It is known that this gelation is due to a reaction between the mercaptans in the oil and copper from the brass fittings which leads to the formation of oil insoluble copper mercaptides. Copper mercaptides derived from long chain aliphatic mercaptans, e.g. n-dodecanethiol, have an ability to effect gelation of the oil medium. The resulting gel is commonly called mercaptide gel. The present invention, by the use of t-alkylammonium t-alkyldithiocarbamates, prevents the mercaptide gel formation as well as precipitation of the copper mercaptide.
Fuel oils, particularly non-hydrofined furnace fuel oils, also have a tendency to form color and sediment when stored exposed to the air. The formation of sediment is particularly undesirable since it eventually effects plugging of line filters and fine orifices, such as burner nozzles and fuel injectors. The present invention, by use of t-alkylamrnonium t-alkyldithiocarbamates, will inhibit sediment formation in the fuel oils being stored.
The particular t-alkylamrnonium t-alkyldithiocarbamates of the present invention can be synthesized by slowly adding one mole of carbon disulfide to two moles of a tertiary alkyl primary amine, in which the alkyl group is highly branched. The number of carbon atoms in the alkyl group of the primary amine ranges from about 8 to 30 but the preferred range is from about 12 to 22. The reaction temperature is maintained in the range from about 25 C. to 35 C., preferably at a temperature of about 30 C. The following reaction occurs:
2t-RNHz-l-CSz t-RNHii-smaNR-tp The yield is essentially 100% Any excess carbon disulfide is easily removed by evaporation at room temperature under reduced pressure, for example, 200 mm. of Hg. The resulting additive is easily dissolved in suitable solvents such as benzene, xylene, or ethanol, in order to obtain a convenient stock solution which is added to the fuel oil in an appropriate amount.
The amount of t-alkylammonium t-alkyldithiocarbamates used may vary depending upon the particular base oil as, for example, in the range from about 0.0001 to 05 wt. percent, preferably in the range from about 0.005 to 0.1 wt. percent based on the oil.
The important requirement of the t-alkylammonium t-alkyldithiocarbamates is that they be of the following type:
That is, that there be no hydrogen atom on the carbon atom attached directly to the nitrogen. R is any alkyl group which must be branched. A few typical members of this class of compounds are: l,l,3,3-tetramethyl butylammonium, 1,1,3,3-tetramethylbutyldithiocarbamate, and 1,l,3,3,5,5 hexamethylhexylammonium l,1,3,3,5,5-hexamethylhexyldithiocarbamate.
The alkyl groups of the amines used in the synthesis of the additive can be obtained through olefin polymerization using BF The resulting olefin is a complex mixture, which is rather undefinable as olefin tetramers. Consequently, the conversion of these olefin polymers to amines will also afford rather undefinable amine mixtures. Nevertheless, these amines, because of their branchiness, hence increased oil solubility, are preferably used for the synthesis of t-alkylammonium t-alkyldithiocarbamates. Such amines are commercially available and are commonly referred to as Prirnene 8l-R and Primene J.M.T.
Also, the t-alkylammonium t-alkyldithiocarbamates of the present invention should have molecular weights ranging from about 334 to about 950 but preferably from about 446 to about 726.
Typical distillate fuels boiling in the range from 250 to 750 F. to which the present additives may be added are middle distillate heating oils. These fuels are of commercial grade and have typical properties as follows.
Composition:
Straight run gas oil -percent 50 Cat. cracked gas oil do 50 Inspections:
Gravity, API 28.7 ASTM pour, F., no additive +20 Viscosity, centistokes at 100 F. 3.60 Distillation ASTM, F.-
I.B.P 308 10% 466 50% 560 628 =F.B.P 670 In order to further illustrate the invention, a number of tests were conducted as illustrated in the fol-lowing examples.
EXAMPLE 1 Suitable concentrations of oil soluble copper compounds; that is, cupric naphthenate and an aliphatic mercaptan, i.e. n-dodecanethiol, when added to fuel oils will effect a gelation of the oil. The elfect of the talkyldithiocarbamate on this gelation is shown in the following table. In each of these tests a copper naphthenate solution was added to a solution of the mercaptan and talkyl-ammonium t-alkyldithiocarbamate mixture.
Table I.Effect of t-alkylammonium t-alkyldithiocarbamate n gelation (a) Additive structure 1 (b) Each solution contained 0.007 gram mole/liter of cupric naphthenate and 0.028 gram mole/liter of n-dodecanethiol in 25 ml. of a furnace fuel oil.
Additive added mole/ liter: Remarks Nil Rapid gelation of the oil with slight precipitation after 16 hours.
0.0006 No gelation but slight precipitation after 2 hours.
0.00138 Same as above.
0.00422 No gelation and no precipitation.
0.0055 8 Same as above.
0.00965 No gelation but slight turbidity noted.
1A mixture of (312-014 t-alkyl primary amine Was used to synthesize the additive.
From Table I it is evident that in the absence of the additive there is a gelation of the oil. However, in the presence of the additive there is no gelation. When the additive concentration is nearly equal to the copper concentration 0.00422 and 0.007 gram mole/liter respectively, there is no gelation, no precipitation and no observable change. At lower additive concentration there is no gelation but there is precipitation. Addition of larger amounts of additive similarly prevent gelations. However, at 0.00965 mole/liter additive concentration there appeared a slight turbidity but no precipitation.
EXAMPLE 2 An accelerated test was devised to simulate field conditions to demonstrate the effect of the additive on mercapticle gel formation on an actual copper surface.
Copper strips (7X 1.0 cm.) were specially corroded by first polishing with emery cloth, then storing for 24 hours in an ammonia saturated benzene solution. The saturated solution was prepared by shaking benzene with concentrated ammonia solution then separating the henzene layer. The corroded copper strips were then gently wiped, washed in pertoleum ether and air dried before weighing. These copper strips were then suspended in one liter 1:1 blends of lye washed cat. cracked and straight run gas oils. The tests ran at 10 C. for eight hours then room temperature for two days.
Four test solutions of different constituency were made Solution: Composition I Fuel oil blend originally containing 8.4 mg. of mercaptan sulphur per 100 ml. of oil.
II Fuel oil blend with an added 2:221 mixture of n-hexadecyl, n-dodecyl and 2-naphthyl mercaptan. The total mercaptan sulphur concentrations was 114 mg./ 100 ml.
III Same composition as solution II except added 0.01 wt./vol. percent of additive. 1
IV I Same composition as solution II except added 0.1 wt./vol. percent of additive. 1
Additive from reaction of carbon disulphide with a mix ture of Caz-C14 t-alkyl primary amines.
After the aforementioned storage period, the copper strips were gently washed in petroleum ether then air dried. The dried strips were then weighed. The test results are given in Table II.
1 T able II Copper strip Change in weight Remarks from solution of strip (mg) 1.. Nil. No visible change.
II +14.7 A green-yellow gelatinous coating of the strip was formed.
III +109- Same as II.
IV- Nil. Slight darkening of strip.
The above result-s clearly show the antigel-ation propenty of the additive.
EXAMPLE 3 Two 121 blends of lye washed cat. cracked gas oil and straight run gas oil were aerated at 20 C. at the rate of 100 cc./minute. To one oil, 0.01% of t-alkylammonium t-alkyldithiocarbamate was added. The dithiocarbamate used here was made by the reaction of carbon disulphide with a mixture of C C t-alkyl primary amines, by the aforementioned synthesis procedure. During the aerations, the ASTM colors of the solutions were determined. The results are given below:
Table 111 ASTM colors Additive added Nil 0.01%
Aeration time (days):
The results show that the additive slightly improves the color stability of the fuel oil over a definite period of time, after which the color degrades to the level of the uninhibited oil.
EXAMPLE 4 The additive used in these tests was the same as that used in the tests of Example 3. Two oil blends were prepared. Blend A was 4:1 mixture of cat. cracked gas oil and straight run gas oil while Blend B was a 1:1 mixture of the two oils. Each oil used in making the blends had been previously lye washed. Various concentrations of additive were added to the blends, then the resulting solutions were stored in the dark for six weeks in wide mouth open bottles at 43 C. The experimental results are given in Table IV.
1 Starting color was less than 1.0. 2 After 6 weeks storage.
The amount of sediment was determined in each case by filtration through a fine sintered glass filtering crucible, washing the collected sediment with n-heptane, then drying at C. and weighing when dried.
The results show that the additive has a marked effect in decreasing the sediment formation in the furnace fuel oils. The effect is particularly noticeable in the very unstable Blend A, which contains mostly cracked materials.
Thus, the present invention is concerned with reducing the mercaptide gel formation of hydrocarbon compositions, particularly fuel oil compositions. The invention is particularly applicable to those hydrocarbon compositions having mercaptan numbers above about 10, particularly in the range of from about 10 to 100. However, the invention is also effective in reducing the tendency for gel formation even on oils having mercaptan numbers in the range from about 4 to 10. It is preferred that the additive concentration approach the concentration of the copper concentration, as for example that the additive concentration be above 50% of the copper concentration.
What is claimed is:
1. A hydrocarbon fuel oil composition consisting essentially of a major quantity of a hydrocarbon fuel oil containing mercaptans and from 0.0001 to 0.5% by weight based upon the total composition of a t-alkylammonium t-alkyldithiocarbamate having a structural formula as References Cited by the Examiner UNITED STATES PATENTS 2,251,686 8/1941 Musselman et a1. 252402 2,343,393 3/1944 Bergen 252-402 2,912,314 11/1959 Geller et a1. 4472 DANIEL E. WYMAN, Primary Examiner.

Claims (1)

1. A HYDROCARBON FUEL OIL COMPOSITION CONSISTING ESSENTIALLY OF A MAJOR QUANTITY OF A HYDROCARBON FUEL OIL CONTAINING MERCAPTANS AND FROM 0.0001 TO 0.5% BY WEIGHT BASED UPON THE TOTAL COMPOSITION OF A T-ALKYLAMMONIUM T-ALKYLDITHIOCARBAMATE HAVING A STRUCTURAL FORMULA AS FOLLOWS:
US226741A 1962-09-27 1962-09-27 Fuel oils Expired - Lifetime US3238026A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US226741A US3238026A (en) 1962-09-27 1962-09-27 Fuel oils

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US226741A US3238026A (en) 1962-09-27 1962-09-27 Fuel oils

Publications (1)

Publication Number Publication Date
US3238026A true US3238026A (en) 1966-03-01

Family

ID=22850212

Family Applications (1)

Application Number Title Priority Date Filing Date
US226741A Expired - Lifetime US3238026A (en) 1962-09-27 1962-09-27 Fuel oils

Country Status (1)

Country Link
US (1) US3238026A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2251686A (en) * 1939-09-28 1941-08-05 Standard Oil Co Lubricating compound
US2343393A (en) * 1940-12-19 1944-03-07 Phillips Petroleum Co Lubricant
US2912314A (en) * 1956-05-01 1959-11-10 Du Pont Cracked fuel oils stabilized with amine salts of dithiocarbamic acids

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2251686A (en) * 1939-09-28 1941-08-05 Standard Oil Co Lubricating compound
US2343393A (en) * 1940-12-19 1944-03-07 Phillips Petroleum Co Lubricant
US2912314A (en) * 1956-05-01 1959-11-10 Du Pont Cracked fuel oils stabilized with amine salts of dithiocarbamic acids

Similar Documents

Publication Publication Date Title
US2657984A (en) Fuel oils
US3035907A (en) Hydrocarbon composition containing an itaconic acid-amine reaction product
US3387954A (en) Liquid hydrocarbon fuels containing a quaternary ammonium compound
US3158647A (en) Quaternary ammonium fatty, phenate and naphthenate salts
US3493508A (en) Organic compositions containing metal salts of reaction product of an alkyl phenol and an ethyleneamine
US3652242A (en) Liquid hydrocarbon fuels containing alkylamine salts
US3309182A (en) Polyether diamine as stabilizer for petroleum distillate fuels
US2913413A (en) Compositions for engine operation
US3038791A (en) Phenyl phosphate compositions
US2697033A (en) Stable fuel oil compositions
US3092475A (en) Fuel composition
US3238026A (en) Fuel oils
US2261227A (en) Compression ignition engine fuels
US2842433A (en) Motor fuel composition
US2959915A (en) Fuel for and method of operating a jet engine
US2230844A (en) High octane number motor fuel
US2385158A (en) Hydrocarbon fuel blends
US3416903A (en) Thermally stable fuel compositions
US2905541A (en) Stable distillate fuel oil compositions
US3365477A (en) Alkoxy metal salts of succinamic acids
US2626208A (en) Preparation of stable distillate fuels from cracked stocks
US3506712A (en) Quaternary amine salts useful as fuel stabilizers
US2943924A (en) Stable fuel oil compositions
US3261674A (en) Stabilized gasoline antiknock compositions and gasoline containing same
US2899459A (en) Salts of z