US2691572A - High sulfur diesel fuel containing organic lead salts - Google Patents

High sulfur diesel fuel containing organic lead salts Download PDF

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US2691572A
US2691572A US135507A US13550749A US2691572A US 2691572 A US2691572 A US 2691572A US 135507 A US135507 A US 135507A US 13550749 A US13550749 A US 13550749A US 2691572 A US2691572 A US 2691572A
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lead
fuel
sulfur
weight
diesel
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Primo L Pinotti
Maurice R Barusch
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California Research LLC
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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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/08Use of additives to fuels or fires for particular purposes for improving lubricity; for reducing wear
    • 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
    • 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 a fuel for use in compression ignition engines, .in particular to .a diesel fuel consisting essentially of a petroleum distillate characterized by a high sulfur content above about 0.5% by weight and especially above 1.0% by weight and by a boiling range lying within the temperature rangeabout 350-750 F., and a minor amount of an oil-soluble lead compound selected from the group consisting of lead naphthenates and lead sulfonates, sufficient to substantially decrease the engine wear incident to the combustion of the fuel.
  • the base fuels which are employed in the composition may be broadly described as petroleum distillates boiling in the range about 350-750 F., having a high sulfur content above about 0.5% by weight, and having an A. P. I. gravity above 20 and ordinarily above 25.
  • the sulfur compounds are predominantly sulfides, disulfides and thiophenes; the more reactive sulfur compound such as mercaptans usually are removed from the fuel by a sweetening process. Distillates boiling in this range and having an even higher sulfur content, for example above 1.0% by weight, are especially suitable for use in the composition.
  • Thoroughly acceptable fuels for use in engines in service requiring frequent speed and low changes, such as automotive diesel engines may be prepared by employing more volatile distillates such as distillates boiling in the range about 350-625 F.
  • the base fuel may suitably be a straight run distillate of a high sulfur crude such as a West Texas crude oil or a Santa Maria crude oil. Blends of straight run and cracked distillates having high sulfur contents may also be used as the base fuel in the composition.
  • a number of oil-soluble lead naphthenates, lead sulfonates, and lead salts of fatty acids have been incorporated in diesel fuels and tested to determine their effect on the rate of engine wear. It appears that all oil-soluble lead naphthenates, lead sulfonates and lead salts of fatty acids are effective in reducing engine wear, but it is preferred to employ compounds of high molecular Weight such as lead salts of high molecular weight acids such as sulfonic acids having molecular weights above about 400 and of naphthenic acids having molecular weights above about 225.
  • the lead sulfonates which are employed in the composition of this invention are lead salts of sulfonic acids prepared by sulfonating such materials as white oils, lubricating oil fractions, higher boiling fractions of S02 extracts of gas oils, and high boiling synthetic alkyl aryl compounds such as those prepared by alkylating benzene with propylene polymers or with butylene polymers or with mixed propylene-butylene polymers.
  • the sulfonic acids preferably have molecular weights above about 400 so that the resulting lead sulfonates have high solubilities in oil and relatively little solubility in water.
  • the lead sulfonates may be prepared by heating litharge and the sulfonic acids while agitating the mixture.
  • the sulfonates may also be prepared by contacting the sulfonate of an alkali metal or of an alkaline earth metal in solution in a paraffinic oil with aqueous lead nitrate and alcohol.
  • aqueous lead nitrate and alcohol For example, 1300 grams of calcium sulfonate prepared from a sulfonic acid having a molecular weight above 400 was dissolved in 2 liters of a parafinic petroleum distillate boiling in the range 185290 F. The calcium sulfonate sample contained about 50% of unsulfonated oil.
  • the solution of sulfonate in the petroleum distillate was washed with 200 milliliters of 190 proof ethyl alcohol and 546 grams of lead nitrate dissolved in 700 cc. of water.
  • the lead nitrate solution and the calcium sulfonate solution were agitated withsteam for a period of about minutes.
  • the mixture was allowed to stand and an upper oily phase and a lower aqueous phase separated.
  • the oily phase containing the dissolved sulfonates was subjected to three additional treatments with lead nitrate solution, the amounts and method of contact being the same as those just described.
  • the oily phase separated from the final contact with lead nitrate was washed with ethyl alcohol and water.
  • a small amount of lead oxide was added to the oily phase to neutralize any residual acidic material and the oily phase was permitted to stand on a steam plate overnight.
  • the oily phase was then topped at 350 F. under 8 millimeters pressure to remove the paraflinic solvent.
  • a lead sulfonate concentrate was recovered which was suitable for use in the fuel composition of this invention.
  • the lead naphthenates which are employed in the composition of this invention may be prepared in the following manner: A straight-run distillate from a naphthenic crude oil, for example a heavy gas oil having a molecular weight in the range 260-270, is washed with dilute caustic such as 3-8 B. caustic. An aqueous phase containing sodium naphthenate is separated when the washing is complete. This aqueous phase is treated with 98% sulfuric acid to separate an oily phase comprising naphthenic acids and an aqueous phase comprising sodium sulfate. The oily phase is separated and distilled under a vacuum to separate non-acidic materials from the naphthenic acids.
  • a naphthenic crude oil for example a heavy gas oil having a molecular weight in the range 260-270
  • the naphthenic acids are heated to a temperature in the range 250-300 F. and litharge is slowly stirred into the acid at this temperature. After the addition of litharge has been completed the mixture is held at temperature for approximately half an hour. The mixture is then cooled and a low boiling petroleum distillate such as Stoddard solvent is added to dissolve the lead naphthenates. The solution is then filtered and the filtrate comprising a solution of lead naphthenates is recovered as a product. The solvent is added in such amount that the lead content of the solution is in the range about 20-28% by weight. This solution is added to the diesel fuel to produce the composition of this invention.
  • the lead salts of fatty acids which may be employed in the composition are lead oleate, lead palmitate, lead stearate and the like or lead soaps produced from unrefined fats.
  • the methods of producing these materials are well known.
  • Lead naphthenates, lead sulfonates or lead salts of fatty acids are added to the base fuel in amounts suflicient to give the compounded fuel a lead content in the range 0.005-0.07% by weight; however, it is preferred to employ an amount of lead naphthenate or lead sulfonate sufficient to give the compounded fuel a lead content in the range 0.02-0.06% by weight. If the amount of these materials added to the base fuel is below that necessary to make the lead content at least as high as 0.005% by weight, relatively little effect on the wear characteristics of the fuel is observed.
  • Example 1 Two parallel tests were run. In one test a diesel fuel was burned without the addition of a lead sulfonate or naphthenate and the wear rate incident to its combustion was measured. In a second parallel run the same diesel fuel was employed, but lead naphthenate was added to the fuel in amount sufficient to give the fuel a lead content of 1.8 10- pound atoms per gallon, which would correspond to 0.053 lead by weight Cetane number
  • the tests were conducted in a single cylinder Caterpillar diesel engine. Operating conditions during the tests were:
  • Example 2 The base fuel described in Example 1 was employed in the runs of this example. In the first run the fuel alone was burned and the wear rate was determined by the method described in Example 1. In the second run the base fuel containing lead sulfonate in an amount sufficient to give the compounded fuel a lead content of 0.053% by weight was burned and the wear rate was determined.
  • the lead sulfonate employed in this example was prepared by alkylating benzene with polypropylene, a heavy alkane fraction boiling in the range about 625-750 F. was separated, this fraction was sulfonated with concentrated sulfuric acid, and the resulting sulfonic acid was neutralized with sodium hydroxide. The sodium sulfonate was reacted with lead nitrate to separate lead sulfonate which was added to the base fuel. The wear rate of the fuel containing lead sulfonate was 44% of that of the base fuel without the additive.
  • Example 3 The runs of Example 2 were repeated, but the lead containing additive employed in this example was a basic lead sulfonate prepared by reacting the alkane sulfonic acid of Example 2 with a stoichiometric excess of litharge to produce a basic lead sulfonate.
  • the wear rate of the fuel containing basic lead sulfonate in amount sufiicient to give the compounded fuel a lead content of 0.053 was 42% of that of the base fuel without any additive.
  • Example 4 Two 240-hour tests under operating conditions typical of field service (rated load and 175 F. water jacket) in a Caterpillar 13-4400 engine were conducted. In one test a West Coaststraight run diesel fuel was burned, and in the second test the same West Coast straight run diesel fuel containing added lead naphthenate in amount suflicient to give the compounded fuel a lead content of 0.053% was burned.
  • the diesel fuel had the following inspections:
  • Example 5 A West Coast straight run diesel fuel having a sulfur content of 3.36% was burned in a diesel engine with and without the addition of lead naphthenate. In both tests the engine was operated at a jacket temperature of 175 F., a sump temperature of 150 F., and an exhaust temperature of 800 F. When the fuel was burned without the addition of lead naphthenate, the wear rate of 2.15 milligrams per hour was observed. When the fuel was burned with lead naphthenate added in amount sufficient to give the fuel a lead content of 1.8 pound atoms of lead per gallon, the wear rate was 1.45 milligrams per hour.
  • the appended drawing is a graphical representation of data obtained during numerous runs in which diesel fuels having sulfur contents ranging from 0.7% by weight to 2.0% by weight and containing lead naphthenate in varying amounts were burned.
  • the graphs clearly show the effectiveness of lead naphthenate in reducing engine wear incident to the combustion of diesel fuels having high sulfur contents above about 0.5% by Weight. It is clear from the graphs that the addition of lead naphthenate in amount sufficient to give the diesel fuel a lead content of at least 0.01% by weight produces a significant reduction in engine wear. It is clear from the graphs that the addition of lead naphthenate in amounts beyond that necessary to give the fuel a lead content of about 0.06% by weight results in relatively little incremental wear reduction.
  • lead naphthenate Since the addition of larger quantities of lead naphthenate to the fuel tends to increase engine deposits, it is preferred to use lead naphthenate in amount not exceeding that necessary to give the fuel a lead content of 0.06% by weight of lead; the addition of lead naphthenate in this amount gives substantially all of the wear reduction which it is possible to obtain by adding lead naphthenate to the fuel, and as indicated in Example 4 above the addition of lead naphthenate in this amount has no adverse effect on engine cleanliness.
  • a high-sulfur diesel fuel of improved wear characteristics comprising a diesel fuel oil boiling Within the range of about 350 F. to about 750 F. having an API gravity above about 20 and characterized by the presence of at least 0.5% by weight of sulfur contained therein in the form of stably bound naturally occurring sulfur compounds and between about 0.005 and 0.07 weight per cent of lead in the form of oil-soluble lead compounds selected from the group consisting of naphthenates, sulfonates, and high molecular weight salts of fatty acids having about 14 to about 18 carbon atoms per molecule.
  • a high-sulfur diesel fuel of improved wear characteristics comprising a diesel fuel oil boiling within the range of about 350 F. to about 750 F. having an API gravity above about 20 and characterized by the presence of at least 0.5% by weight sulfur contained therein in the form of stably bound naturally occurring sulfur compounds and between about 0.005 and 0.0? weight per cent of leadin the form of an oilsoluble lead naphthenate having a molecular weight above about 225.
  • a high-sulfur diesel fuel of improved wear characteristics comprising a diesel fuel oil boiling within the range of about 350 F. to about 750 F. having an API gravity above about 20 and characterized by the presence of at least 0.5% by weight of sulfur contained therein in the form of stably bound naturally occurring sulfur compounds and between about 0.005 and 0.07 weight per cent of lead in the form of an oil-soluble lead sulfonate having a molecular weight above about 400.

Description

Oct. 12, 1954 RELATIVE WEAR RATE PERCENT I80 EFFECT OF ADDITIVE CONCENTRATION I ONIRELATIVE RING WIEARI RA E I l l I I I l SINGLE CYLINDER -43" BORE CATERPILLAR usmc RADIOACTIVE RINGS 115% SULFUR FUEL=I0O 1 REL. WEAR RATE I75F.JACKET TEMP.
I50F. SUMP TEMP. I40 |4oo R.P.M.
3.54 LBS./HR. FUEL FLOW '30 1 (APPROX.-IO0 v.
RATED LOAD) +-2.o% s. FUEL I20 e-|.|5% s. FUEL 0.1m s. FUEL ||o -F so 7o 6o w 0 so e 40 R P. L. PINOTTI ETAL 2,691,572 HIGH SULFUR nmssx. FUELCONTAINING ORGANIC LEAD SALTS Filed June 28, 1949 0 0.0l 0.02 0.03 0.04 0.05 0.06 0.07 0.08 0.09 0.l0 0.ll
PERCENT LEAD BY WT. AS LEAD NAPHTHENATE INVENTORS P'rimo L. Pinorri Maurice R. Barysch Patented Oct. 12, 1954 HIGH SULFUR DIESEL FUEL CONTAINING IORGANIC LEAD'SALTS Primo L. Pinotti, Larkspur, and Maurice R.
Barusch, Richmond, Califl, assignors to California Research Corporation, San Francisco, Calif., a corporation of Delaware Application December 28, 1949, Serial No.-135,507
4 Claims.
This invention relates to a fuel for use in compression ignition engines, .in particular to .a diesel fuel consisting essentially of a petroleum distillate characterized by a high sulfur content above about 0.5% by weight and especially above 1.0% by weight and by a boiling range lying within the temperature rangeabout 350-750 F., and a minor amount of an oil-soluble lead compound selected from the group consisting of lead naphthenates and lead sulfonates, sufficient to substantially decrease the engine wear incident to the combustion of the fuel.
It is recognized in the literature that engine Wear rates are increased markedly'as the sulfur content of the fuel rises. This increase in vvear is attributed to the corrosive action of the combustion products of the sulfur compounds contained in the fuel on the interior metallic surfaces of the engine. Recognition of this effect of sulfur compounds in the fuel has led to the setting up of fairly rigid specifications in respect to sulfur content in diesel fuels. For example, in ASTM Standards on Petroleum Products and Lubricants, November 1948, published by the American Society for Testing Materials, tentative specifications for diesel fuel oils are set out at pages 548 and 549. For a volatile distillate fuel oil for engines in service requiring frequent speed and load changes such as an automotive diesel engine a maximum sulfur content of 0.50% by weight is specified. For distillate fuels of low volatility for engines in industrial and heavy -mobile service a maximum sulfur content of 1.0% isspecified. In the'appended comments onthe standards set out in the AS'IMspecifications for diesel fuels it is stated that the effect of sulfur content on engine wear appears to vary considerably in importance depending on engine design and operating conditions, and that in order to make available the widest range of fuels the permissible sulfur contents were specified at as high a value as practicable. Various manufacturers of diesel engines supply their customers with recommended fuel specifications. These recommendations include such specifications as a maximum sulfur content of 0.25% for diesel-fuels for winter use in high speed automotive engines and a maximum sulfur content of 1% for some railroad diesel engines.
In consequence of the established effect of sulfur compounds in diesel fuels on engine Wear and the various relatively low maximum sulfur contents which have been recommended for diesel fuels, petroleum refiners have-been forced tomarket large volumes of diesel .fuelshaving low sulfur content, for examplerwell below-0.5% by Weight. In order ,to meet these specifications, many stocks must be either treated at considerable expense to reduce sulfur content or their use in diesel fuel must be avoided. During the past several years the ratio of high sulfur crude oil refined to total crude oil refined has very markedly increased. This trend, coupled with the fairly rigid diesel;fuel specifications for sulfur, presents the petroleum refiner with a serious problem of determining how high-sulfur, middle-of-the-barrel fractions may be economically utilized.
It is the paramount object of this invention to provide a diesel engine :fuel composition in which high sulfur petroleum distillates may be used without first subjecting them to expensive desulfurization processes.
It is a further object of this invention to provide a diesel fuel having a high sulfur content which may be burned in internal combustion engines without producing the high. engine wear rates which are ordinarily observed when high sulfur fuels are burned.
It has been found that the addition of a minor amount of an oil-soluble lead salt of an organic acid or of an organo-inorganic acid to a petroleum distillate boiling in the boiling .range of diesel fuels and having'a high sulfur content such as above 0.5% by weight or especially above 1.0% by weight produces very marked reductions in engine wear when thefuel containing the lead compound is burned. v
The marked reduction in engine wear observed when lead naphthenatesare introduced into'the fuel is not accompaniedby any increase in engine deposits even thoughno lead scavenger is used. This is rather unexpected in the light of past experience with spark ignition engines in which gasoline containing tetraethyl lead has been burned. The gasolineexperience has been that no appreciable alteration in wear rate is observed by the addition of tetraethyl lead alone and that engine deposits are noticeably increased. To'offset the engine deposit problem created by the introduction of tetraethyl lead, various lead scavengers have been added to the fuel. The introduction of these materials reduces'the engine deposits which would accompany the combustion of the fuel containing tetraethyl lead alone, but their introduction is accompanied by a small but definite increase in wearrate. When oil-solublelead naphthenates or .sulfonates or lead salts of fattyacids are added ,to heavier stocks having sulfur contents 3 much higher than those which are encountered in leaded gasolines, marked decreases in engine wear are observed without any accompanying increase in engine deposits even though no scavenger for lead is employed.
The base fuels which are employed in the composition may be broadly described as petroleum distillates boiling in the range about 350-750 F., having a high sulfur content above about 0.5% by weight, and having an A. P. I. gravity above 20 and ordinarily above 25. The sulfur compounds are predominantly sulfides, disulfides and thiophenes; the more reactive sulfur compound such as mercaptans usually are removed from the fuel by a sweetening process. Distillates boiling in this range and having an even higher sulfur content, for example above 1.0% by weight, are especially suitable for use in the composition. Thoroughly acceptable fuels for use in engines in service requiring frequent speed and low changes, such as automotive diesel engines, may be prepared by employing more volatile distillates such as distillates boiling in the range about 350-625 F. and having sulfur content in excess of 0.5% by weight in the composition of the invention. The base fuel may suitably be a straight run distillate of a high sulfur crude such as a West Texas crude oil or a Santa Maria crude oil. Blends of straight run and cracked distillates having high sulfur contents may also be used as the base fuel in the composition.
A number of oil-soluble lead naphthenates, lead sulfonates, and lead salts of fatty acids have been incorporated in diesel fuels and tested to determine their effect on the rate of engine wear. It appears that all oil-soluble lead naphthenates, lead sulfonates and lead salts of fatty acids are effective in reducing engine wear, but it is preferred to employ compounds of high molecular Weight such as lead salts of high molecular weight acids such as sulfonic acids having molecular weights above about 400 and of naphthenic acids having molecular weights above about 225.
The lead sulfonates which are employed in the composition of this invention are lead salts of sulfonic acids prepared by sulfonating such materials as white oils, lubricating oil fractions, higher boiling fractions of S02 extracts of gas oils, and high boiling synthetic alkyl aryl compounds such as those prepared by alkylating benzene with propylene polymers or with butylene polymers or with mixed propylene-butylene polymers. The sulfonic acids preferably have molecular weights above about 400 so that the resulting lead sulfonates have high solubilities in oil and relatively little solubility in water. The lead sulfonates may be prepared by heating litharge and the sulfonic acids while agitating the mixture. The sulfonates may also be prepared by contacting the sulfonate of an alkali metal or of an alkaline earth metal in solution in a paraffinic oil with aqueous lead nitrate and alcohol. For example, 1300 grams of calcium sulfonate prepared from a sulfonic acid having a molecular weight above 400 was dissolved in 2 liters of a parafinic petroleum distillate boiling in the range 185290 F. The calcium sulfonate sample contained about 50% of unsulfonated oil. The solution of sulfonate in the petroleum distillate was washed with 200 milliliters of 190 proof ethyl alcohol and 546 grams of lead nitrate dissolved in 700 cc. of water. The lead nitrate solution and the calcium sulfonate solution were agitated withsteam for a period of about minutes. The mixture was allowed to stand and an upper oily phase and a lower aqueous phase separated. The oily phase containing the dissolved sulfonates was subjected to three additional treatments with lead nitrate solution, the amounts and method of contact being the same as those just described. The oily phase separated from the final contact with lead nitrate was washed with ethyl alcohol and water. A small amount of lead oxide was added to the oily phase to neutralize any residual acidic material and the oily phase was permitted to stand on a steam plate overnight. The oily phase was then topped at 350 F. under 8 millimeters pressure to remove the paraflinic solvent. A lead sulfonate concentrate was recovered which was suitable for use in the fuel composition of this invention.
The lead naphthenates which are employed in the composition of this invention may be prepared in the following manner: A straight-run distillate from a naphthenic crude oil, for example a heavy gas oil having a molecular weight in the range 260-270, is washed with dilute caustic such as 3-8 B. caustic. An aqueous phase containing sodium naphthenate is separated when the washing is complete. This aqueous phase is treated with 98% sulfuric acid to separate an oily phase comprising naphthenic acids and an aqueous phase comprising sodium sulfate. The oily phase is separated and distilled under a vacuum to separate non-acidic materials from the naphthenic acids. The naphthenic acids are heated to a temperature in the range 250-300 F. and litharge is slowly stirred into the acid at this temperature. After the addition of litharge has been completed the mixture is held at temperature for approximately half an hour. The mixture is then cooled and a low boiling petroleum distillate such as Stoddard solvent is added to dissolve the lead naphthenates. The solution is then filtered and the filtrate comprising a solution of lead naphthenates is recovered as a product. The solvent is added in such amount that the lead content of the solution is in the range about 20-28% by weight. This solution is added to the diesel fuel to produce the composition of this invention.
The lead salts of fatty acids which may be employed in the composition are lead oleate, lead palmitate, lead stearate and the like or lead soaps produced from unrefined fats. The methods of producing these materials are well known.
Lead naphthenates, lead sulfonates or lead salts of fatty acids are added to the base fuel in amounts suflicient to give the compounded fuel a lead content in the range 0.005-0.07% by weight; however, it is preferred to employ an amount of lead naphthenate or lead sulfonate sufficient to give the compounded fuel a lead content in the range 0.02-0.06% by weight. If the amount of these materials added to the base fuel is below that necessary to make the lead content at least as high as 0.005% by weight, relatively little effect on the wear characteristics of the fuel is observed. When the amount of lead sulfonate or lead naphthenate added to the fuel is in excess of that required to give the compounded fuel a lead content of 0.07%, the excess lead produces relatively little incremental effect on the rate of engine wear irrespective of the sulfur content of the fuel, and in addition a tendency toward heavier engine deposits during operation is observed. The effectiveness of the lead sulfonates and the lead naphthenates to reduce engine wear incident to the combustion of diesel fuels, especially high sulfur diesel fuels, is illustrated by the following examples.
Example 1 Two parallel tests were run. In one test a diesel fuel was burned without the addition of a lead sulfonate or naphthenate and the wear rate incident to its combustion was measured. In a second parallel run the same diesel fuel was employed, but lead naphthenate was added to the fuel in amount sufficient to give the fuel a lead content of 1.8 10- pound atoms per gallon, which would correspond to 0.053 lead by weight Cetane number The tests were conducted in a single cylinder Caterpillar diesel engine. Operating conditions during the tests were:
Jacket temperature F 175 Sump temperature F 150 Exhaust temperature F' 800 The pistons were equipped with radioactive piston rings and wear rates were obtained by determining the radioactivity of the lubricating oil employed with a Geiger counter. This method of determining wear rates has been published appearing in the S. A. E. Journal, June 1949, at page 52. The validity and reliability of this method of determining wear have been fully established by checking and coordinating the results obtainedin this type of test with those obtained with the same fuels in conventional tests for determining engine wear which are characterized by long periods of engine operation such as 200-400 hours, and direct measurements of engine wear. The wear rate in the test in which diesel fuel containing lead naphthenate was burned was found to be 40% of the wear rate observed when the diesel fuel without lead naphthenate was burned.
Example 2 The base fuel described in Example 1 was employed in the runs of this example. In the first run the fuel alone was burned and the wear rate was determined by the method described in Example 1. In the second run the base fuel containing lead sulfonate in an amount sufficient to give the compounded fuel a lead content of 0.053% by weight was burned and the wear rate was determined. The lead sulfonate employed in this example was prepared by alkylating benzene with polypropylene, a heavy alkane fraction boiling in the range about 625-750 F. was separated, this fraction was sulfonated with concentrated sulfuric acid, and the resulting sulfonic acid was neutralized with sodium hydroxide. The sodium sulfonate was reacted with lead nitrate to separate lead sulfonate which was added to the base fuel. The wear rate of the fuel containing lead sulfonate was 44% of that of the base fuel without the additive.
6 Emample 3 The runs of Example 2 were repeated, but the lead containing additive employed in this example was a basic lead sulfonate prepared by reacting the alkane sulfonic acid of Example 2 with a stoichiometric excess of litharge to produce a basic lead sulfonate. The wear rate of the fuel containing basic lead sulfonate in amount sufiicient to give the compounded fuel a lead content of 0.053 was 42% of that of the base fuel without any additive.
Example 4 Two 240-hour tests under operating conditions typical of field service (rated load and 175 F. water jacket) in a Caterpillar 13-4400 engine were conducted. In one test a West Coaststraight run diesel fuel was burned, and in the second test the same West Coast straight run diesel fuel containing added lead naphthenate in amount suflicient to give the compounded fuel a lead content of 0.053% was burned. The diesel fuel had the following inspections:
Gravity A. P. I. 32.8 Viscosity SSU at 100 F. 34.5 Sulfur, weight per cent 1.00 Conradson carbon 10% bottoms, weight per cent 0.05 Color ASTM 1% Flash, P. M., F. 168 Neutralization number 0.03 Cetane number 45.4 Distillation ASTM D-158:
Start F 360 10% F.. 417 30% F 454 50% F 492 70% F 532 F 592' F 630 End point F 685 The lead naphthenate was pr p in the manner described in Example 1 and had the fol lowin properties:
Lead content, Weight percent 24.0. Non-volatile residue, weight percent 64.0. Flash point, tag open cup F 110. Appearance Clear. Color Gardiner 8.
Comparative wea-r data for these two runs are presented in the following table:
West Coast Diesel Straight Fuel Run Sulfur, percent 1. 0 1.0 Lead by wt. as Lead Naphthenate, percent 0. 00 0. 053 Top Ring Wt. Loss, mg./hr. 2. 0 1.18 Top Ring Wear, perceut 40. 5 Cyl. Liner Wear, in./l,000 hr 0.0069 0.0033 Oyl. Liner Wear, percent 1 100 47. 8
Base fuel assigned 100% wear rate.
it clearly appeared thatthefuel containing lead naphthenate was at least equal to the base fuel in respect to engine cleanliness.
It is known that lead naphthenates, when used in lubricating oils without the addition of inhibitors, accelerate bearing corrosion with both copper-lead and cadmium-silver bearings. In order to determine whether the employment of lead naphthenate in a diesel fuel adversely affected copper-lead bearing corrosion, the fresh lubricat-' ing oil and lubricating oil which had been used in 240-hour tests in a Caterpillar D-4400 engine burning a 1% sulfur fuel with and without the addition of lead naphthenate were tested in the 300 F. accelerated copper-lead strip corrosion test. The results obtained are tabulated below:
These data indicate that lead naphthenate when added to the fuel and burned normally in the engine does not contribute to the corrosion of copper-lead bearings since the results obtained are similar and within the reproducibility of the test which is :33 milligrams. The corrosivity of the lead naphthenate in the lubricating oil is indicated by the high strip weight loss obtained in test No. 4 in the above table.
Example 5 A West Coast straight run diesel fuel having a sulfur content of 3.36% was burned in a diesel engine with and without the addition of lead naphthenate. In both tests the engine was operated at a jacket temperature of 175 F., a sump temperature of 150 F., and an exhaust temperature of 800 F. When the fuel was burned without the addition of lead naphthenate, the wear rate of 2.15 milligrams per hour was observed. When the fuel was burned with lead naphthenate added in amount sufficient to give the fuel a lead content of 1.8 pound atoms of lead per gallon, the wear rate was 1.45 milligrams per hour.
The appended drawing is a graphical representation of data obtained during numerous runs in which diesel fuels having sulfur contents ranging from 0.7% by weight to 2.0% by weight and containing lead naphthenate in varying amounts were burned. The graphs clearly show the effectiveness of lead naphthenate in reducing engine wear incident to the combustion of diesel fuels having high sulfur contents above about 0.5% by Weight. It is clear from the graphs that the addition of lead naphthenate in amount sufficient to give the diesel fuel a lead content of at least 0.01% by weight produces a significant reduction in engine wear. It is clear from the graphs that the addition of lead naphthenate in amounts beyond that necessary to give the fuel a lead content of about 0.06% by weight results in relatively little incremental wear reduction. It will be observed thata diesel fuel having leadnaph thenate present in amount to give the fuel a lead content of 0.1% by weight is just slightly better than a diesel fuel containing lead naphthenate in amount suiiicient to give the fuel a lead content of 0.05% by weight in respect to engine wear rate. Since the addition of larger quantities of lead naphthenate to the fuel tends to increase engine deposits, it is preferred to use lead naphthenate in amount not exceeding that necessary to give the fuel a lead content of 0.06% by weight of lead; the addition of lead naphthenate in this amount gives substantially all of the wear reduction which it is possible to obtain by adding lead naphthenate to the fuel, and as indicated in Example 4 above the addition of lead naphthenate in this amount has no adverse effect on engine cleanliness.
We'elaim:
l. A high-sulfur diesel fuel of improved wear characteristics comprising a diesel fuel oil boiling Within the range of about 350 F. to about 750 F. having an API gravity above about 20 and characterized by the presence of at least 0.5% by weight of sulfur contained therein in the form of stably bound naturally occurring sulfur compounds and between about 0.005 and 0.07 weight per cent of lead in the form of oil-soluble lead compounds selected from the group consisting of naphthenates, sulfonates, and high molecular weight salts of fatty acids having about 14 to about 18 carbon atoms per molecule.
2. The fuel as defined by claim 1, wherein said weight per cent sulfur is at least 1.0 weight per cent.
3. A high-sulfur diesel fuel of improved wear characteristics comprising a diesel fuel oil boiling within the range of about 350 F. to about 750 F. having an API gravity above about 20 and characterized by the presence of at least 0.5% by weight sulfur contained therein in the form of stably bound naturally occurring sulfur compounds and between about 0.005 and 0.0? weight per cent of leadin the form of an oilsoluble lead naphthenate having a molecular weight above about 225.
4. A high-sulfur diesel fuel of improved wear characteristics comprising a diesel fuel oil boiling within the range of about 350 F. to about 750 F. having an API gravity above about 20 and characterized by the presence of at least 0.5% by weight of sulfur contained therein in the form of stably bound naturally occurring sulfur compounds and between about 0.005 and 0.07 weight per cent of lead in the form of an oil-soluble lead sulfonate having a molecular weight above about 400.
References Cited in the file of this patent UNITED STATES PATENTS Number Name Date 2,045,788 Maverick June 30, 1936 2,230,642 Fischer et al Feb. 4, 1941 2,575,003 Caron et al Nov. 13, 1951 FOREIGN PATENTS Number Country Date 561,328 Great Britain May 15, 1944 599,222 Great Britain Mar. 8, 1948

Claims (1)

1. A HIGH-SULFUR DIESEL FUEL OF IMPROVED WEAR CHARACTERISTICS COMPRISING A DIESEL FUEL OIL BOILING WITHIN THE RANGE OF ABOUT 350* F. TO ABOUT 750* F. HAVING AN API GRAVITY ABOVE ABOUT 20* AND CHARACTERIZED BY THE PRESENCE OF AT LEAST 0.5% BY WEIGHT OF SULFUR CONTAINED THEREIN IN THE FORM OF STABLY BOUND NATURALLY OCCURRING SULFUR COMPOUNDS AND BETWEEN ABOUT 0.005 AND 0.07 WEIGHT PER CENT OF LEAD IN THE FORM OF OIL-SOLUBLE LEAD COMPOUNDS SELECTED FROM THE GROUP CONSISTING OF NAPHTHENATES, SULFONATES, AND HIGH MOLECULAR WEIGHT SALTS OF FATTY ACIDS HAVING ABOUT 14 TO ABOUT 18 CARBON ATOMS PER MOLECULE.
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2789892A (en) * 1952-10-22 1957-04-23 California Research Corp Diesel fuel composition
DE1077358B (en) * 1957-08-22 1960-03-10 Exxon Research Engineering Co Heating oil
US3341310A (en) * 1958-09-26 1967-09-12 Torrimetal Trust Fuels for internal combustion engines
DE1545266B1 (en) * 1966-04-27 1969-10-16 Dasic Chemicals Ltd Compensation for heavy heating oils with a high sulfur content

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE556943A (en) * 1956-05-03

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US2045788A (en) * 1933-07-11 1936-06-30 Standard Oil Dev Co Fuel for high pressure liquid fuel injection engines
US2230642A (en) * 1938-08-13 1941-02-04 Standard Oil Dev Co Fuel oil
GB561328A (en) * 1941-07-05 1944-05-15 Standard Oil Dev Co Improvements relating to fuel oils
GB599222A (en) * 1945-09-21 1948-03-08 Anglo Iranian Oil Co Ltd Improvements relating to motor fuels
US2575003A (en) * 1948-07-03 1951-11-13 Shell Dev Fuel oil composition

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2045788A (en) * 1933-07-11 1936-06-30 Standard Oil Dev Co Fuel for high pressure liquid fuel injection engines
US2230642A (en) * 1938-08-13 1941-02-04 Standard Oil Dev Co Fuel oil
GB561328A (en) * 1941-07-05 1944-05-15 Standard Oil Dev Co Improvements relating to fuel oils
GB599222A (en) * 1945-09-21 1948-03-08 Anglo Iranian Oil Co Ltd Improvements relating to motor fuels
US2575003A (en) * 1948-07-03 1951-11-13 Shell Dev Fuel oil composition

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2789892A (en) * 1952-10-22 1957-04-23 California Research Corp Diesel fuel composition
DE1077358B (en) * 1957-08-22 1960-03-10 Exxon Research Engineering Co Heating oil
US3341310A (en) * 1958-09-26 1967-09-12 Torrimetal Trust Fuels for internal combustion engines
DE1545266B1 (en) * 1966-04-27 1969-10-16 Dasic Chemicals Ltd Compensation for heavy heating oils with a high sulfur content

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