US2534309A - Composition for internal-combustion engines - Google Patents

Composition for internal-combustion engines Download PDF

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US2534309A
US2534309A US784519A US78451947A US2534309A US 2534309 A US2534309 A US 2534309A US 784519 A US784519 A US 784519A US 78451947 A US78451947 A US 78451947A US 2534309 A US2534309 A US 2534309A
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hydroperoxide
gasoline
engine
compression
composition
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Donald H Sheffield
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Hercules Powder Co
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/1811Organic compounds containing oxygen peroxides; ozonides

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  • This invention relates to an improvement in the ignition and combustion characteristics of gasoline as a fuel for internal combustion engines, and to the prevention and the removal of carbon and gum deposits from the combustion chambers of internal combustion engines.
  • liquid organic solvents are ethyl alcohol, furfuryl alcohol, kerosene, coal oil, carbon tetrachloride, chloroform, benzene, toluene, xylene, the various liquid terpene hydrocarbons, and organic esters, ethers, ketones, amines and amides.
  • Numerous mixtures of such solvents also have been proposed. Many of-these reagents have exerted a limited beneficial effect on the operation of internal combustion engines, but they have generally been unsatisfactory due to incomplete removal of carbon and gum deposits and in not effecting the desired result; namely, a significant increase in compression.
  • compositions comprising an a,adialkylarylmethyl hydroperoxide and gasoline not only will act as an improved fuel but also will be of utility in removing deposits of carbon and gum efficiently and economically.
  • the compositions of this invention give added power to internal combustion engines, effect a cleaner combustion in that carbon formation is decreased, and facilitate gradual removal of carbon deposit already present.
  • the compositions remove carbon and gum deposits from the combustion chambers of the engines and, barring mechanical faults in the engines, restore the compression of the engines to a normal level.
  • carbon and gum deposits may be removed from an internal combustion engine by the process of admitting a gasoline solution of an a,a-dialkylarylmethyl hydroperoxide, such as a,a-dlll'lethylbenzyl hydroperoxide, to the combustion chambers of the engine through the usual fuel system, including the carburetor, while the engine is running under normal operating conditions.
  • the solution also may be formed, then added to the engine by introducing the hydroperoxide through the air intake of the carburetor while the engine is running at idling speed.
  • the solution of the hydroperoxide in gasoline is formed within the carburetor.
  • the engine speed may be accelerated to effect removal of the loosened deposits through the exhaust.
  • the a,a-dialkylarylmethyl hydroperoxide used in this example was a,-dimethylbenzy1 hydroperoxide, obtained by the air oxidation of 011- mene in the liquid phase in the presence of aqueous sodium hydroxide.
  • the a,a-dimethylbenzyl hydroperoxide was used in the form of the reaction product obtained by the air oxidation.
  • This reaction product contained 46.3% by weight of the hydro-peroxide, the balance of product being primarily a,a-dimethylbenzyl alcohol and cumene, but also containing a small amount of acetophenone.
  • the cylinder head was removed from a six-cylinder International motor, and it was found that the motor contained a moderate carbon deposit and a considerable deposit of gummy material. Upon replacement of the cylinder head the motor was warmed up to normal running temperature and the compression in each cylinder determined. The motor then was run at a moderate speed while 250 ml. of the a,a-dimethylbenzyl hydroperoxide-containing reaction product was added rapidly directly into the carburetor air intake, the rate being such that the motor did not quite choke down. Following addition of the hydroperoxide, the motor was run at a moderate speed for 10 minutes, then the compression of each cylinder was again determined. It was observed that the spark plugs had been cleaned as a result of the hydroperoxide addition. The motor then was run at a moderate speed on 0.9 gallon of gasoline in which was dissolved 31 ml. of
  • a six-cylinder Continental motor was warmed up to normal running temperature and the compression in each cylinder determined. The motor then was run at a moderate speed while 250 ml. of the a,a-dimethylbenzyl hydroperoxide-com taining reaction product used in Example 1 was rapidly introduced through the carburetor air intake. The motor was run at a moderate speed for 10 minutes following addition of the hydroperoxide, then the compression of each cylinder again was determined. The results of each compression test are given in Table II.
  • a six-cylinder Mack motor was warmed up to normal running temperatureand the compression in each cylinder determined. The motor then was run on 1.0 gallon of gasoline containing, per gallon, 273 ml. of the a,a-dimethylbenzyl hydroperoxide-containing reaction product utilized in Example 1, the gasoline solution being added through the fuel line leading into the carburetor. The compression of each cylinder again was determined. The results are given in Table IV.
  • EXAMPLE 6 Using the 72.8% a,a-dimethylbenzyl hydroperoxide product of Example 5, a six-cylinder Oak engine was subjected to a purging operation. The initial compression of each cylinder was determined, then 107.7 mi. of the 72.8% hydroperoxide product was added through the carburetor air intake while the engine was running at idling speed. The engine then was operated at 2000 R. P. M. on 0.5 gallon of gasoline containing 26.9 ml. of the hydroperoxide product per gallon, the gasoline solution being added through the fuel line leading into the carburetor. The 107.7 mi. hydroperoxide addition and the hydroperoxide-gasoline feed steps then were repeated, after which the compression of each cylinder again was determined. The compression data are shown in Table V.
  • the com- EXAMPLE 8 pression of the cylinders in each engine was h aaa yl lm hyl hydrop -x us d measured both before and after the test while in this example was a,a-dimethyl-p-methylbenzyl the engine was running at normal operating temhy p ro de Obtained y the x dat o f P- 40 perature. The results of the tests are given in cymene in the liquid phase in the presence of r me x. aqueous sodium hydroxide using molecular oxy- T ble X gen.
  • the a,a-dimethyl-p-methylbenzyl hydroperoxide was used in the form of the reaction whim Dodge Chevrolet product obtained by the oxidation.
  • This reaction product contained 36.9% by weight of the Amouft hydropergxide (my) ganon hydroperoxide. ine
  • Such hydroperoxides may be prepared by the oxidation of alkyl-substituted aromatic organic compounds having the structural formula in which R1 and R: represent alkyl groups and Ar represents a substituent selected from the group consisting of aryl and alkaryl groups.
  • the oxidation may be carried out in the liquid phase utilizing air or molecular oxygen as the 7 in the presence of an aqueous alkali.
  • the concentration of the aqueous alkali may be between about 1% and about 35% although it is preferable to use concentrations of about 2% to about 8%. Vigorous agitation is desirable during the oxidation reaction.
  • the a,a-dialkylarylmethyl hydroperoxides used in accordance with this invention have the following structural formula in which R1 and R2 represent alkyl groups, Ar represents a substituent selected from the group consisting of aryl and alkaryl groups and X represents the hydroperoxy (-0011) group.
  • R1 and R2 represent alkyl groups
  • Ar represents a substituent selected from the group consisting of aryl and alkaryl groups
  • X represents the hydroperoxy (-0011) group.
  • alkyl-substituted aromatic organic compounds which may be oxidized
  • pcymene cumene
  • diisopropylbenzene may be mentioned. These compounds lead to G,d-d1- methyl-p-methylbenzyl, a,v.-dimethylbenzyl, and a,a-dimethyl-p-isopropylbenzyl hydroperoxides, respectively.
  • a,a,a',a'-tetlamethylp-xylylene dihydroperoxide there may be obtained a,a,a',a'-tetlamethylp-xylylene dihydroperoxide.
  • These compounds also may be named as aryl(dialkyl)methyl hydroperoxides; for example, a,a-dimethylbenzyl hydroperoxide may be designated as phenyl(dimethyDmethyl hydroperoxide.
  • the aryl and alkaryl groups need not be derived from benzene, as is the case in the afore-mentioned compounds, for compounds containing aromatic nuclei derived from naphthalene, anthracene, phenanthrene, and the like also are operable when dissolved in a suitable solvent during the oxidation.
  • the aryl group may be substituted with alkyl groups such as methyl, ethyl, propyl, isopropyl, butyl, isobutyl, secondary butyl, tertiary butyl, and the like, to give alkaryl substituents, the same alkyl groups also being rep- I resentative of R1 and R2 in the structural formula.
  • R1 and R: may be either the same or different.
  • compositions comprising an a,a-dialkylarylmethyl hydroperoxide and gasoline may be prepared using several different modifications of the hydroperoxide material.
  • the hydroperoxide may be used, for example, either in the form of the pure hydroperoxide, or in the form of a crude reaction mixture containing the hydroperoxide and obtained by the oxidation with air or oxygen of an alkyl-substituted aromatic organic compound having the structural formula shown previously.
  • the hydroperoxide is obtained by such an oxidation, the oxidation usually is interrupted before all of the hydrocarbon has reacted in order to avoid or limit side reactions.
  • the a,a-dialkylarylmethyl hydroperoxide is obtained in mixture with smaller or larger amounts of the original hydrocarbon, which is an a,a-dialkylarylmethane, and the mixture also may contain secondary reaction products such as the corresponding alcohols, which are a,a-dialkylarylmethyl alcohols.
  • the oxidation of cumene leads to a reaction product containing ,c-dimethylbenzyl hydroperoxide, a,a-dimethylbenzyl alcohol, a small amount of acetophenone, and unchanged cumene.
  • Such a reaction product may be used per se in forming the gasoline-hydroperoxide compositions of this invention.
  • the hydroperoxide may be separated from the other constituents of the crude reaction mixture.
  • the hydroperoxides may be separated from the reaction mixtures by, for example, fractional distillation at very low pressures, of
  • the hydroperoxides having higher boiling points than the related hydrocarbon, alcohol and ketone.
  • the hydroperoxides also may be separated from the oxidation reaction mixtures by crystallization, which may be facilitated by first distilling off at least part of the hydrocarbon. Steam distillation usually is sufficient to remove the hydrocarbon.
  • the concentration of the gasoline and the c,a-dialkylarylmethyl hydroperoxide in the composition comprising the hydroperoxide and gasoline will depend somewhat upon the particular use to which the composition is to be placed.
  • the concentration of gasoline preferably will be at least 10% by weight, based on the total composition, and the remainder of the composition may be the hydroperoxide.
  • the concentration of the hydroperoxide may be varied, however, from about 0.05% to 90% by weight, based on the total composition. Except in the extreme instance in which the composition is composed of 10% gasoline and 90% hydroperoxide by weight, other components may be present in the composition.
  • the concentration of the hydroperoxide may be from about 0.05% to about 10% by weight, based on the total composition, and desirably is from about 0.05% to about 2%. A preferable range on this basis is from about 0.05% to about 1%.
  • the concentration of the hydroperoxide may be from about 10% to 90% by weight, based on the total composition. Preferably the concentration is from about 30% to about and a particularly applicable range is from about 40% to about 70%.
  • the amount of gasoline in the composition therefore may range generally from 10% to about 99.95% by weight, based on the total composition.
  • the amount of gasoline be at least about 75% by weight, based on the total composition, preferably at least about by weight.
  • concentration of gasoline desirably is from about 75% to about 99.95%, and preferably from about 90% to about 99.95%.
  • the simplest procedure involves utilization of the air intake of the carburetor.
  • a solution of the hydroperoxide in gasoline or, for example, a crude oxidation reaction mixture containing the hydroperoxide.
  • a more concentrated solution of the hydroperoxide formed by removing unreacted hydrocarbon from a crude oxidation reaction mixture and there even may be added those pure hydroperoxides which when pure exist as liquids.
  • the pure hydroperoxides it is preferable to dissolve them in gasoline or other suitable solvent prior to addition to the carburetor.
  • solvents such as ethanol, benzene, toluene, xylene, diisopropylbenzene, cumene, cymene, petroleum ether, heptane, and, in general, the nonpolar, volatile hydrocarbons of the parafflnic, naphthenic and aromatic series may be used, in otherwords, to take the hydroperoxide into solution prior to the carburetor addition.
  • Lubricating oils also are advantageous as solvents for the hydroperoxide, and the hydroperoxide may be either in a pure or concentrated form, or in the form of a crude oxidation reaction product. In any of these instances, however, the composition entering the combustion chambers of the internal combustion engine comprises the hydroperoxide and gasoline.
  • compositions in accordance with this invention are easily prepared merely by dissolving the hydroperoxide, in the form of any of the modifications previously discussed, in the gasoline. This may be done, for example, either at the refinery, thereby incorporating the hydroperoxide as one of the original constituents of the fuel as it is to be sold to the consumer, or by adding a certain amount of the hydroperoxide to the engines fuel tank containing a prescribed amount of gasoline.
  • the compositions may be used primarily as fuels or primarily as purging agents depending upon the type of treatment mostrequired by the engine, but, as also shown by the examples, the two types of treatment may be combined with beneficial results.
  • the engine may, for example, first be given a purging treatment with a relatively high hydroperoxide-content composition, then be operated on a fuel composition containing a relatively small amount of hydroperoxide. No matter what the treatment, the most beneficial results are obtained when the engine is being operated at a normal running temperature. With most engines such a temperature is on the order of at least 140' F. and generally is within the range of 140 F. to 180 F.
  • the addition of the hydroperoxide may be as rapid as possible without causing the engine to choke, and upon completion of the addition the speed of the engine may be accelerated in order to expel the loosened carbon and gum deposits out the exhaust.
  • the engine knock present when the motor has excess carbon deposits will be gone and, in general, the performance of the engine will be noticeably improved.
  • the condition of sticky valves caused by gum deposits on the valve stems is remedied and spark plugs are cleaned, improving slow speed performance and idling.
  • the compositions of this invention are superior to other materials suggested by the art in that the hydroperoxide compositions effect a more complete removal of carbon and gum deposits and result in a significant increase in compression.
  • a gasoline fuel containing an a,a-dialky1- arylmethyl hydroperoxide containing an a,a-dialky1- arylmethyl hydroperoxide.
  • a gasoline fuel containing from about 0.05% to about 90% by weight, based on the total composition, of an a,a-dialkyiarylmethyl hydroperoxide.
  • a gasoline fuel containing from about 0.05% to about 10% by weight, based on the total composition, of an a,a-dialkylarylmethyl hydroperoxide.
  • a gasoline fuel containing from about 10% to about 90% by weight, based on the total composition, of an a,a-dialkylarylmethyl hydroperoxide.
  • a gasoline fuel containing an a,a-dialkylarylmethyl hydroperoxide and an a,a-dialkylarylmethyl alcohol.
  • a gasoline fuel containing an a,a-dialkylarylmethyl hydroperoxide, an a,a-dialkylarylmethyl alcohol and an a,a-dialkylarylmethane.
  • a gasoline fuel containing a,a-dimethylbenzyl hydroperoxide containing a,a-dimethylbenzyl hydroperoxide.
  • a gasoline fuel containing a,a-dimethyl-pmethylbenzyl hydroperoxide 8.
  • a gasoline fuel containing a,a-dimethyl-pisopropylbenzyl hydroperoxide a,a-dimethyl-pisopropylbenzyl hydroperoxide.

Description

Patented Dec. 19, 1950 COMPOSITION FOR INTERNAL- COMBUSTION ENGINES Donald H. Sheffield, Wilmington, DeL, assignor to Hercules Powder Company, Wilmington, DeL, a corporation of Delaware No Drawing. Application November 6, 1947, Serial No. 784,519
9 Claims. 1
This invention relates to an improvement in the ignition and combustion characteristics of gasoline as a fuel for internal combustion engines, and to the prevention and the removal of carbon and gum deposits from the combustion chambers of internal combustion engines.
Many materials, such as alcohols, ketones, nitroalkanes and organometallic compounds have been proposed for addition to gasoline to improve the ignition and combustion properties of this fuel. Various methods and reagents also have been suggested for purging the internal parts of an internal combustion engine of accumulated contaminants incident to both the current and past operation of the engine, most of these reagents having been organic liquids having a solvent action on the gummy deposits which retain a good share of the carbon. Exemplary of such liquid organic solvents are ethyl alcohol, furfuryl alcohol, kerosene, coal oil, carbon tetrachloride, chloroform, benzene, toluene, xylene, the various liquid terpene hydrocarbons, and organic esters, ethers, ketones, amines and amides. Numerous mixtures of such solvents also have been proposed. Many of-these reagents have exerted a limited beneficial effect on the operation of internal combustion engines, but they have generally been unsatisfactory due to incomplete removal of carbon and gum deposits and in not effecting the desired result; namely, a significant increase in compression.
Now in accordance with this invention it has been found that a composition comprising an a,adialkylarylmethyl hydroperoxide and gasoline not only will act as an improved fuel but also will be of utility in removing deposits of carbon and gum efficiently and economically. When used as fuels, the compositions of this invention give added power to internal combustion engines, effect a cleaner combustion in that carbon formation is decreased, and facilitate gradual removal of carbon deposit already present. When utilized as purging agents, the compositions remove carbon and gum deposits from the combustion chambers of the engines and, barring mechanical faults in the engines, restore the compression of the engines to a normal level.
As an illustration of the present invention, carbon and gum deposits may be removed from an internal combustion engine by the process of admitting a gasoline solution of an a,a-dialkylarylmethyl hydroperoxide, such as a,a-dlll'lethylbenzyl hydroperoxide, to the combustion chambers of the engine through the usual fuel system, including the carburetor, while the engine is running under normal operating conditions. The solution also may be formed, then added to the engine by introducing the hydroperoxide through the air intake of the carburetor while the engine is running at idling speed. In this instance the solution of the hydroperoxide in gasoline is formed within the carburetor. Upon completion of the addition of the gasoline solution of the hydroperoxide the engine speed may be accelerated to effect removal of the loosened deposits through the exhaust.
The following examples constitute specific embodiments of the invention.
EXAMPLE 1 The a,a-dialkylarylmethyl hydroperoxide used in this example was a,-dimethylbenzy1 hydroperoxide, obtained by the air oxidation of 011- mene in the liquid phase in the presence of aqueous sodium hydroxide. The a,a-dimethylbenzyl hydroperoxide was used in the form of the reaction product obtained by the air oxidation. This reaction product contained 46.3% by weight of the hydro-peroxide, the balance of product being primarily a,a-dimethylbenzyl alcohol and cumene, but also containing a small amount of acetophenone.
The cylinder head was removed from a six-cylinder International motor, and it was found that the motor contained a moderate carbon deposit and a considerable deposit of gummy material. Upon replacement of the cylinder head the motor was warmed up to normal running temperature and the compression in each cylinder determined. The motor then was run at a moderate speed while 250 ml. of the a,a-dimethylbenzyl hydroperoxide-containing reaction product was added rapidly directly into the carburetor air intake, the rate being such that the motor did not quite choke down. Following addition of the hydroperoxide, the motor was run at a moderate speed for 10 minutes, then the compression of each cylinder was again determined. It was observed that the spark plugs had been cleaned as a result of the hydroperoxide addition. The motor then was run at a moderate speed on 0.9 gallon of gasoline in which was dissolved 31 ml. of
the hydroperoxide-containing reaction product per gallon, the gasoline solution being added through the fuel line leading into the carburetor. Again the compression of each cylinder was determined. Removal of the cylinder head showed that the carbon and gum deposits had been effectively removed from the head and the valves, although a small amount of gummy matter reassasoc 3 mained on the pistons. The results of each compression test are given in Table I.
A six-cylinder Continental motor was warmed up to normal running temperature and the compression in each cylinder determined. The motor then was run at a moderate speed while 250 ml. of the a,a-dimethylbenzyl hydroperoxide-com taining reaction product used in Example 1 was rapidly introduced through the carburetor air intake. The motor was run at a moderate speed for 10 minutes following addition of the hydroperoxide, then the compression of each cylinder again was determined. The results of each compression test are given in Table II.
Table II Compression (lbalsq. in.)
Cylinder Number 1 2 3 4 5 0 Titfisaiam'aartaxman: 13? 13? it it? 33 id EXAMPLE 3 The procedure of Example 2 was followed on a six-cylinder Chevrolet motor. The compression data are given in Table III.
Table III Compression (lbeJsq. in.)
CylinderNumber 1 2 3 4 5 6 iitittasasaarraatiaai:::: 1% i% it, ii ii? iii EXAMPLE 4 A six-cylinder Mack motor was warmed up to normal running temperatureand the compression in each cylinder determined. The motor then was run on 1.0 gallon of gasoline containing, per gallon, 273 ml. of the a,a-dimethylbenzyl hydroperoxide-containing reaction product utilized in Example 1, the gasoline solution being added through the fuel line leading into the carburetor. The compression of each cylinder again was determined. The results are given in Table IV.
Table IV Compression (lbs/sq. in.)
Cylinder Number"... 1 2 3 4 5 6 Initial 104 65 75 81 91 114 After Hydroperoxide-Gasoline Feed 11B 100 97 110 114 125 EXAMPLE 5 The a,a-dimethylbenzyi hydroperoxide used in this example was a product which contained 72.8% of the hydroperoxide and which was obtained by the air oxidation of cumene in the liquid phase in the presence of aqueous sodium hydroxide to give a reaction product containing 33% of the hydroperoxide, this reaction product then being steam stripped of unreacted cumene to give the 72.8% product.
An eight-cylinder Buick engine was tested for compression, and all cylinders were found to be 140 lbs/sq. in., indicating that the engine was in excellent condition. However, a considerable carbon deposit was noticed on all spark plugs, consequently 107.7 ml. of the 72.8% hydroperoxide product was added through the carburetor air intake while the engine was running at idling speed. The engine speed then was accelerated to 2000 R. P. M. for 2 minutes. The spark plugs were removed and found to be completely free of carbon.
EXAMPLE 6 Using the 72.8% a,a-dimethylbenzyl hydroperoxide product of Example 5, a six-cylinder Plymouth engine was subjected to a purging operation. The initial compression of each cylinder was determined, then 107.7 mi. of the 72.8% hydroperoxide product was added through the carburetor air intake while the engine was running at idling speed. The engine then was operated at 2000 R. P. M. on 0.5 gallon of gasoline containing 26.9 ml. of the hydroperoxide product per gallon, the gasoline solution being added through the fuel line leading into the carburetor. The 107.7 mi. hydroperoxide addition and the hydroperoxide-gasoline feed steps then were repeated, after which the compression of each cylinder again was determined. The compression data are shown in Table V.
Table V Compression (lbs/sq. in.)
Cylinder Number l 2 3 4 5 6 Initial 80 50 After Hydroperoxide Additions. 105 95 30 EXAMPLE 7 The .-dimethylbenzyl hydroperoxide used in this example was a product which contained 78.4% of the hydroperoxide and which was obtained by the air oxidation of cumene in the liquid phase in the presence of aqueous sodium hydroxide to give a reaction product containing 33% of the hydroperoxide, this reaction product then being steam stripped of unreacted cumene over aqueous sodium hydroxide to give the 78.4% product.
An eight-cylinder V-type Ford engine was warmed up to normal operating temperature and the compression in each cylinder determined. The engine was operated at a fixed throttle setting until the speed became constant. then the engine was run successively on 0.5 gallon of gasoline containing about 26.9 ml. of the 78.4% hydroperoxide product per gallon, 0.5 gallon of gasoline. containing about 53.8 ml. of the 78.4% hydroperoxide product per gallon, and finally on straight gasoline, all additions being made through the fuel line leadinginto the carburetor. The R. P. M. values were observed during each phase of the test, and upon completion of the test the compression of each cylinder again was determined. It was noticed upon completion of the test that the spark plugs were considerably cleaner. The test data are given in Tables VI'and VII.
the air oxidation of cumene in the liquid phase in the presence of aqueous sodium hydroxide.
An Oldsmobile automobile containing an eightcylinder engine was operated under actual driving conditions using six gallons of gasoline in which was dissolved 37.7 ml. of the hydroperoxlde pergallon of gasoline. The automobile then was operated on straight gasoline for an additional 250 miles. The compression of each cylinder of the engine was measured both before and after the test while the engine was running at normal operating temperature. The results of each compression test are given in Table IX.
gine then was operated at idling speed on 0.5 gallon of gasoline containing 29.9 ml. of the hydroperoxide product per gallon. Upon completion of this operation the engine was operated using 0.5 gallon of gasoline containing 59.7 ml. of the hydroperoxide per gallon, after which the compression of each cylinder again was determined. Both hydroperoxide-gaso-line solutions were added through the fuel line leading into The a,a-dimethylbenzyl hydroperoxide used in this example was a product which contained 52% of the hydroperoxide and which was obtained by Table VI Table IX I Compression (IbsJsq. in.) Compression (lbsJsq. in.)
Bightbank Leftbank Cylinder-Number 1 2 a 4 5 e 1 8 Cylinder Number 1 2 a 4 1' 2 a 4 Initial 105 110 110 11 0 no as so 100 Alter hydro roxidegasoline an straight 111111111 101 115 122 120 116 110 114 11c gasollneieeds 10s 11s 11s 113 110 11s 106 105 After hydroperoxide additions 110 no 127 126 121 122 118 121 EXAMPLE 1o Table VII The a,a-dimethylbenzy1 hydroperoxlde used in this example was a product which contained Fuel Engin 43.5% of the hydroperoxide and which was obtained by the air oxidation of cumene in the liquid phase in the presence of aqueous sodium Straight gasoline (initial) l, 210 hydr Xide fig'f.TR???ff-TllfYf'ifTffl'ifi'.52f. 1,320 A d e u k an a Ch vrolet tru k, both Gasoline eentainlnz hydwpemide/ealcontaining six-cylinder engines, were operated gal. 1,330 Straight gasoline (m1) 1,360 under actual drivmg conditions using gasoline in which was dissolved a specified amount of the hydroperoxide er gallon of gasoline. The com- EXAMPLE 8 pression of the cylinders in each engine was h aaa yl lm hyl hydrop -x us d measured both before and after the test while in this example was a,a-dimethyl-p-methylbenzyl the engine was running at normal operating temhy p ro de Obtained y the x dat o f P- 40 perature. The results of the tests are given in cymene in the liquid phase in the presence of r me x. aqueous sodium hydroxide using molecular oxy- T ble X gen. The a,a-dimethyl-p-methylbenzyl hydroperoxide was used in the form of the reaction whim Dodge Chevrolet product obtained by the oxidation. This reaction product contained 36.9% by weight of the Amouft hydropergxide (my) ganon hydroperoxide. ine
3 3 A six-cy nd Chevrolet engine s warmed i hisitir i cii bisiah'jIIIIII'" 113 1%? u to normal running temperature and the com- Average flmlwmpmssion 119 127 pression in each cylinder determined. The en- The compositions used in accordance with this invention have been shown by the examples as involving the use of the hydroperoxides obtained from the oxidation of cumene and p-cymene, but other a,a-dialkylarylmethyl hydroperoxides also are operable. Such hydroperoxides may be prepared by the oxidation of alkyl-substituted aromatic organic compounds having the structural formula in which R1 and R: represent alkyl groups and Ar represents a substituent selected from the group consisting of aryl and alkaryl groups. The oxidation may be carried out in the liquid phase utilizing air or molecular oxygen as the 7 in the presence of an aqueous alkali. The concentration of the aqueous alkali may be between about 1% and about 35% although it is preferable to use concentrations of about 2% to about 8%. Vigorous agitation is desirable during the oxidation reaction.
The a,a-dialkylarylmethyl hydroperoxides used in accordance with this invention have the following structural formula in which R1 and R2 represent alkyl groups, Ar represents a substituent selected from the group consisting of aryl and alkaryl groups and X represents the hydroperoxy (-0011) group. As illustrative of the alkyl-substituted aromatic organic compounds which may be oxidized, pcymene, cumene, and diisopropylbenzene may be mentioned. These compounds lead to G,d-d1- methyl-p-methylbenzyl, a,v.-dimethylbenzyl, and a,a-dimethyl-p-isopropylbenzyl hydroperoxides, respectively. Also in the case of diisopropylbenzene there may be obtained a,a,a',a'-tetlamethylp-xylylene dihydroperoxide. These compounds also may be named as aryl(dialkyl)methyl hydroperoxides; for example, a,a-dimethylbenzyl hydroperoxide may be designated as phenyl(dimethyDmethyl hydroperoxide. The aryl and alkaryl groups need not be derived from benzene, as is the case in the afore-mentioned compounds, for compounds containing aromatic nuclei derived from naphthalene, anthracene, phenanthrene, and the like also are operable when dissolved in a suitable solvent during the oxidation. The aryl group may be substituted with alkyl groups such as methyl, ethyl, propyl, isopropyl, butyl, isobutyl, secondary butyl, tertiary butyl, and the like, to give alkaryl substituents, the same alkyl groups also being rep- I resentative of R1 and R2 in the structural formula. R1 and R: may be either the same or different.
In carrying out this invention the compositions comprising an a,a-dialkylarylmethyl hydroperoxide and gasoline may be prepared using several different modifications of the hydroperoxide material. The hydroperoxide may be used, for example, either in the form of the pure hydroperoxide, or in the form of a crude reaction mixture containing the hydroperoxide and obtained by the oxidation with air or oxygen of an alkyl-substituted aromatic organic compound having the structural formula shown previously. When the hydroperoxide is obtained by such an oxidation, the oxidation usually is interrupted before all of the hydrocarbon has reacted in order to avoid or limit side reactions. In this manner the a,a-dialkylarylmethyl hydroperoxide is obtained in mixture with smaller or larger amounts of the original hydrocarbon, which is an a,a-dialkylarylmethane, and the mixture also may contain secondary reaction products such as the corresponding alcohols, which are a,a-dialkylarylmethyl alcohols. The oxidation of cumene, for example, leads to a reaction product containing ,c-dimethylbenzyl hydroperoxide, a,a-dimethylbenzyl alcohol, a small amount of acetophenone, and unchanged cumene. Such a reaction product may be used per se in forming the gasoline-hydroperoxide compositions of this invention. In case it is desirable, however, to obtain the hydroperoxide in a more concentrated form, the hydroperoxide may be separated from the other constituents of the crude reaction mixture. The hydroperoxides may be separated from the reaction mixtures by, for example, fractional distillation at very low pressures, of
the order of 0.01 to 1.0 mm./sq. cm., the hydroperoxides having higher boiling points than the related hydrocarbon, alcohol and ketone. In some instances the hydroperoxides also may be separated from the oxidation reaction mixtures by crystallization, which may be facilitated by first distilling off at least part of the hydrocarbon. Steam distillation usually is sufficient to remove the hydrocarbon.
The concentration of the gasoline and the c,a-dialkylarylmethyl hydroperoxide in the composition comprising the hydroperoxide and gasoline will depend somewhat upon the particular use to which the composition is to be placed. In general, the concentration of gasoline preferably will be at least 10% by weight, based on the total composition, and the remainder of the composition may be the hydroperoxide. The concentration of the hydroperoxide may be varied, however, from about 0.05% to 90% by weight, based on the total composition. Except in the extreme instance in which the composition is composed of 10% gasoline and 90% hydroperoxide by weight, other components may be present in the composition. When the composition is to be used as a fuel, the concentration of the hydroperoxide may be from about 0.05% to about 10% by weight, based on the total composition, and desirably is from about 0.05% to about 2%. A preferable range on this basis is from about 0.05% to about 1%. When the composition is to be used as a purging agent, the concentration of the hydroperoxide may be from about 10% to 90% by weight, based on the total composition. Preferably the concentration is from about 30% to about and a particularly applicable range is from about 40% to about 70%. The amount of gasoline in the composition therefore may range generally from 10% to about 99.95% by weight, based on the total composition. When'the composition is to be used as a fuel, it is desirable that the amount of gasoline be at least about 75% by weight, based on the total composition, preferably at least about by weight. Thus, in this use of the composition the concentration of gasoline desirably is from about 75% to about 99.95%, and preferably from about 90% to about 99.95%.
In carrying out a purging operation the simplest procedure involves utilization of the air intake of the carburetor. Through the intake there may be added a solution of the hydroperoxide in gasoline, or, for example, a crude oxidation reaction mixture containing the hydroperoxide. There also may be added a more concentrated solution of the hydroperoxide formed by removing unreacted hydrocarbon from a crude oxidation reaction mixture, and there even may be added those pure hydroperoxides which when pure exist as liquids. In the case of the pure hydroperoxides, however, whether liquid or solid, it is preferable to dissolve them in gasoline or other suitable solvent prior to addition to the carburetor. Other solvents, such as ethanol, benzene, toluene, xylene, diisopropylbenzene, cumene, cymene, petroleum ether, heptane, and, in general, the nonpolar, volatile hydrocarbons of the parafflnic, naphthenic and aromatic series may be used, in otherwords, to take the hydroperoxide into solution prior to the carburetor addition. Lubricating oils also are advantageous as solvents for the hydroperoxide, and the hydroperoxide may be either in a pure or concentrated form, or in the form of a crude oxidation reaction product. In any of these instances, however, the composition entering the combustion chambers of the internal combustion engine comprises the hydroperoxide and gasoline. This is due to the fact that gasoline, aS well as the hydroperoxide, enters the carburetor and a mixing of the two components takes place, resulting in the formation of the hydroperoxide-gasoline composition. The final concentration of the hydroperoxide in the composition in this instance will depend to a great extent on the original concentration of the hydroperoxide in the material added to the carburetor, since the amount of gasoline being fed through the carburetor at any one time may be relatively low in comparison to the amount of hydroperoxide.
When used as fuels the compositions in accordance with this invention are easily prepared merely by dissolving the hydroperoxide, in the form of any of the modifications previously discussed, in the gasoline. This may be done, for example, either at the refinery, thereby incorporating the hydroperoxide as one of the original constituents of the fuel as it is to be sold to the consumer, or by adding a certain amount of the hydroperoxide to the engines fuel tank containing a prescribed amount of gasoline.
As shown by the examples, the compositions may be used primarily as fuels or primarily as purging agents depending upon the type of treatment mostrequired by the engine, but, as also shown by the examples, the two types of treatment may be combined with beneficial results. The engine may, for example, first be given a purging treatment with a relatively high hydroperoxide-content composition, then be operated on a fuel composition containing a relatively small amount of hydroperoxide. No matter what the treatment, the most beneficial results are obtained when the engine is being operated at a normal running temperature. With most engines such a temperature is on the order of at least 140' F. and generally is within the range of 140 F. to 180 F. During a purging operation the addition of the hydroperoxide may be as rapid as possible without causing the engine to choke, and upon completion of the addition the speed of the engine may be accelerated in order to expel the loosened carbon and gum deposits out the exhaust.
By practicing this invention the engine knock present when the motor has excess carbon deposits will be gone and, in general, the performance of the engine will be noticeably improved. The condition of sticky valves caused by gum deposits on the valve stems is remedied and spark plugs are cleaned, improving slow speed performance and idling. The compositions of this invention are superior to other materials suggested by the art in that the hydroperoxide compositions effect a more complete removal of carbon and gum deposits and result in a significant increase in compression.
What I claim and desire to protect by Letters Patent is:
l. A gasoline fuel containing an a,a-dialky1- arylmethyl hydroperoxide.
2. A gasoline fuel containing from about 0.05% to about 90% by weight, based on the total composition, of an a,a-dialkyiarylmethyl hydroperoxide.
3. A gasoline fuel containing from about 0.05% to about 10% by weight, based on the total composition, of an a,a-dialkylarylmethyl hydroperoxide.
4. A gasoline fuel containing from about 10% to about 90% by weight, based on the total composition, of an a,a-dialkylarylmethyl hydroperoxide.
5. A gasoline fuel containing an a,a-dialkylarylmethyl hydroperoxide and an a,a-dialkylarylmethyl alcohol.
6. A gasoline fuel containing an a,a-dialkylarylmethyl hydroperoxide, an a,a-dialkylarylmethyl alcohol and an a,a-dialkylarylmethane.
'7. A gasoline fuel containing a,a-dimethylbenzyl hydroperoxide.
8. A gasoline fuel containing a,a-dimethyl-pmethylbenzyl hydroperoxide.
9. A gasoline fuel containing a,a-dimethyl-pisopropylbenzyl hydroperoxide.
DONALD H. SI-IEFFIEED.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 929,503 Selden July 27, 1909 1,766,501 Buerk June 24, 1930 2,403,772 Vaughan et a1. July 9, 1946

Claims (1)

  1. 2. A GASOLINE FUEL CONTAINING FROM ABOUT 0.05% TO ABOUT 90% BY WEIGHT, BASED ON THE TOTAL COMPOSITION, OF AN A,A-DIALKYLARYLMETHYL HYDROPEROXIDE.
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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2609279A (en) * 1949-11-26 1952-09-02 Standard Oil Dev Co Turbojet fuel
US2698512A (en) * 1949-04-04 1955-01-04 Phillips Petroleum Co Method of operating ram-jet engines
US2715611A (en) * 1950-06-23 1955-08-16 Monsanto Chemicals Air deodorant
US2757207A (en) * 1951-03-20 1956-07-31 Hercules Powder Co Ltd alpha, alpha-dimethylnaphthylmethyl hydroperoxides
US2785662A (en) * 1953-04-06 1957-03-19 Leonard D Boyce Compositions and methods for removing deposits
US2891851A (en) * 1956-07-20 1959-06-23 Shell Dev Fuel for internal combustion engines
US4406254A (en) * 1982-02-10 1983-09-27 General Motors Corporation Method for lean operation of spark-ignited gasoline-fueled reciprocating engine
WO1986000088A1 (en) * 1984-06-15 1986-01-03 George Holcom Kitchen Fuel additive

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US929503A (en) * 1909-05-13 1909-07-27 George B Selden Fuel.
US1766501A (en) * 1926-05-04 1930-06-24 Charles A Buerk Liquid combustible
US2403772A (en) * 1943-11-15 1946-07-09 Shell Dev Production of organic hydroperoxides

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US929503A (en) * 1909-05-13 1909-07-27 George B Selden Fuel.
US1766501A (en) * 1926-05-04 1930-06-24 Charles A Buerk Liquid combustible
US2403772A (en) * 1943-11-15 1946-07-09 Shell Dev Production of organic hydroperoxides

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2698512A (en) * 1949-04-04 1955-01-04 Phillips Petroleum Co Method of operating ram-jet engines
US2609279A (en) * 1949-11-26 1952-09-02 Standard Oil Dev Co Turbojet fuel
US2715611A (en) * 1950-06-23 1955-08-16 Monsanto Chemicals Air deodorant
US2757207A (en) * 1951-03-20 1956-07-31 Hercules Powder Co Ltd alpha, alpha-dimethylnaphthylmethyl hydroperoxides
US2785662A (en) * 1953-04-06 1957-03-19 Leonard D Boyce Compositions and methods for removing deposits
US2891851A (en) * 1956-07-20 1959-06-23 Shell Dev Fuel for internal combustion engines
US4406254A (en) * 1982-02-10 1983-09-27 General Motors Corporation Method for lean operation of spark-ignited gasoline-fueled reciprocating engine
WO1986000088A1 (en) * 1984-06-15 1986-01-03 George Holcom Kitchen Fuel additive
US4609379A (en) * 1984-06-15 1986-09-02 Kitchen Iii George H Fuel additive

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