FUEL LUBRICITY ADDITIVES

Abstract: There is disclosed a fuel lubricity additive, made by a two-step process wherein the first step is co-reacting an unsatured base oil, predominantly from vegetable oil sources, and a compound having a diene structure and a carboxylic acid group, wherein the second step is esterifying or amidifying the free carboxylic acid group of anhydride group with a polyhydroxy-containing compound or polyamine compound to form the final fuel lubricity additive useful in diesel fuels. The inventive fuel lubricity additive also is useful as a dispersant.

Description: FUEL LUBRICITY ADDITIVES Technical Field of the Invention The present invention provides a fuel lubπcity additive, made by a two-step process wherein the first step is co-reacting an unsaturated base oil, predominantly from vegetable oil sources, and a compound having a diene structure and a carboxylic acid group, wherein the second step is esterifying or amidafying the free carboxylic acid group or groups with a polyhydroxy-containing compound or poly-amine compound to form the final fuel lubπcity additive useful in diesel fuels The fuel lubπcity additive formulations and compositions have further utility as dispersants Background of the Invention Beginning m 1993, all highway diesel fuel in the United States was required to have a minimum sulfur content of 0 05% (by weight) Refmeπes have been able to meet this standard by hydrotreatmg Hydrotreatmg removes sulfur, nitrogen and other metal-bonding reactive sites as well as seal-swelling and lubπcatmg aromatic compounds However, a major drawback to the hydrotreatmg process used to reduce sulfur and aromatic levels is that the diesel fuel product has reduced fuel lubncity The reduced fuel lubπcity increases wear rates in many fuel injection systems, as such injections systems have been designed to utilize natural lubπcatmg properties of traditional diesel fuels (typically containing 0 2 to 0 5% by weight sulfur or 2000-5000 ppm) This has caused a dramatic increase in fuel injection system problems manifest as underrun and stalling as the most minor to injector nozzle fouling, to fuel pump failures resulting in a need to replace entire systems This is causing fuel injection systems to be redesigned even as injection pressures have πsen to the detπment of wear and mechanical performance Distillate petroleum hydrocarbon fractions in the kerosene/diesel fuel range have essentially no lubπcity or lubπcatmg value The high solvent action of the fuel and the constant washing by large volumes of fuel make it impossible to maintain lubπcant on pump surfaces Thus, fuel pumps are subjected to seπous wear, leading to pump failure Fuel compositions have to be treated (formulated) to address wear, erosion and corrosion problems Petroleum refineπes produce 50 to 60 billion gallons of diesel fuel for consumption m the United States each year Most refineπes are producing only low-sulfur diesel fuels to achieve economies of scale This means that, even though off-road vehicles are currently exempt from the low-sulfur emission requirements, most, including tractor and other farm equipment, will be using low-sulfur diesel fuels This will result in increased engine wear m agπcultural equipment that was designed for the natural lubπcatmg properties of diesel fuels The EPA is in the process of developing emission standards for off-road engines that will also cause low-sulfur diesel fuels to be used Traditional fuel lubπcity additives contain sulfur, phosphorous, zinc, nitrogen or boron These are called ash forming or catalyst-poisoning additives Ash forming additives are thermally activated and form sacπficial chemical bonds to metal surfaces The additives will then "shear" from the metal surface before the metal itself, resulting in protection of the metal surface from wear Many additives also contπbute to particulate emissions duπng combustion Moreover, additives can form SO x , NO x and PO x emissions, or emissions which can poison a catalyst used in catalytic converters, causing an increase in particulate and hydrocarbon emissions Therefore there is a need in the art for diesel fuel additives that impart needed lubπcity properties but provide minimal ash or preferably ash-less properties for the purposes of reducing ultimate emissions characteπstics The present invention applies telomer technology to this field of art to provide an improved ashless additive to diesel fuel and kerosene that provides lubπcity properties, improved combustion and improved emissions characteπstics The goal, that was achieved by this invention, was to provide a fullv fuel-soluble additive molecule, which is deπved from renewable sources and contains no ash or deposit-producing elements or catalyst poisons such as sulfur, phosphorous or boron The invention descπbes the achievement of that goal Summary of the Invention The present invention provides a fuel lubπcity additive compound, compπsmg an intermediate adduct of a first moiety reacted in a first reaction with a second moiety to form the intermediate adduct and further esteπfymg or amidafying the intermediate adduct with a third moiety m a molar ratio of from about 1 2 to about 2 1 , wherein the first moiety is an unsaturated tπglyceπde plant oil or a thermal polymer thereof, wherein the second moiety is a diene or conjugated carbon-carbon double bond acid or anhydπde moiety, wherein the first reaction compπses mixing the first moiety with the second moiety in a molar ratio of from about 1 2 to about 2 1 at a temperature of from about 130 °C to about 195 °C under an inert atmosphere, and wherein the third moiety is a polyhydroxy compound or a polyammo compound Preferably, the unsaturated plant oil is selected from the group consisting of rapeseed oil, tung oil, lmseed oil, soya oil, corn oil, peanut oil, canola oil, safflower oil, or combinations thereof Preferably, the thermal polymer is selected from the group consisting of thermal (telomer) polymers of canola oil, soya oil, lmseed oil, corn oil, safflower oil, peanut oil, tung oil, and combinations thereof Preferably, the second moiety compπses unsaturated compounds having a free carboxylic acid or anhydπde group Most preferably, the second moiety is selected from the group consisting of maleic acid, maleic anhydπde, sorbic acid, sorbic anhydπde, tetrahydrophfhahc anhydπde, tetrahydrophthahc acid, salicylic acid, salicylic anhydπde, acrylic acid, acrylic anhydπde, Ci ιo alkyl, C? ιo alkenyl, or Ci ιo alkoxy deπvatives of the foregoing acids and anhydπdes, and combinations thereof Preferably, the polyhydroxy compound of the third moiety is selected from the group consisting of glycerol, sorbitol, hydroxyqumone, glucose, mannose, 6-carbon sugars, pentose, fructose, 5-carbon sugars, pentaerythπtol, catechol, resorcinol, hydroqumone, pyrogallol, 4,4'-dιhydroxybιphenyl, 2,4- dihydroxybφhenyl, 2,2'-dιhydroxybιphenyl, orthohydroxybenzene, polyhydroxyaromatic compounds having one or two phenyl πngs and one or two 5-6 membered aromatic πngs having substituted alkyl or alkenyl side chains (C 2 j 0 ) substituted with at least two hydroxyl groups, tπmethylolpropane, pentaerythπtol, dimethylolpropane, dipentaerythπtol, tπmethylolethane, ethyleneglycol, polypropyleneglycol, polyethylated alcohols, and combinations thereof Preferably, the polyamino compound is selected from the group consisting of diethylenetnamme, dimethylenetπamme, dipropylnetπamme, ethyenediamine, propylenediamine, butylenediam e, butylenetπamme, tπethylenetetramme, tπpropylenetetramme, tπmethylenetπamme, tπbutylenetetramme, tetraethylenepentamme, tetramethylenepentamme, tetrapropylenepentamme, tetraethylenepentamme, tetrabutylenepentamme, hexylenediamine. and combinations thereof Preferably, the first reaction is conducted under continuous mixing Preferably, the esteπfication reaction compπses reaction conditions of from about 150 °C to about 190 °C under an inert atmosphere and further compπses adding an esteπfication catalyst Most preferably, the esteπfication catalyst is an acid catalyst Most preferably, the esteπfication catalyst is selected from the group consisting of p-toluene sulfomc acid, hydrophosphorous acid, sulfuπc acid, hydrochloπc acid, phosphoπc acid, acid-activated clays, solid acid catalysts, acidic zeolites, and combinations thereof Preferably, the amidification reaction compπses reaction conditions of from about 130 °C to about 150 °C under an inert atmosphere Most preferably, the fuel lubπcity additive compound is made from the first moiety, second moiety and third moiety compounds selected from the group consisting of in order soya oil-maleic anhydπde-sorbitol, soya oil-lmseed oil combmation-maleic anhydπde-sorbitol, soya oil-maleic anhydπde- efhylenediamine, and soya oil-maleic anhydπde-hydroqumone The present invention further provides a process for synthesizing a fuel lubπcity additive compound, compπsing (a) reacting an unsaturated tπglyceπde plant oil or a thermal polymer thereof first moiety with a second moiety in a molar ratio of from about 1 2 to about 2 1 at a temperature of from about 130 °C to about 195 °C under an inert atmosphere to form an intermediate adduct, wherein the second moiety is a diene or conjugated carbon-carbon double bond acid or anhydπde moiety, and (b) esteπfymg or amidifying the intermediate adduct with a third moiety in a molar ratio of from about 1 2 to about 2 1, wherein the third moiety is a polyhydroxy compound or a polyamino compound Preferably, the unsaturated plant oil is selected from the group consisting of rapeseed oil, tung oil, lmseed oil, soya oil, corn oil, peanut oil, canola oil, safflower oil, or combinations thereof Preferably, the thermal polymer is selected from the group consisting of thermal (telomer) polymers of canola oil, soya oil, lmseed oil, corn oil, safflower oil, peanut oil, tung oil, and combinations thereof. Preferably, the second moiety comprises unsaturated compounds having a free carboxylic acid or anhydride group. Most preferably, the second moiety is selected from the group consisting of maleic acid, maleic anhydride, sorbic acid, sorbic anhydride, tetrahydrophthalic anhydride, tetrahydrophthalic acid, salicylic acid, salicylic anhydride, acrylic acid, acrylic anhydride, Cι_ιo alkyl, C 2- ιo alkenyl, or Ci-io alkoxy derivatives of the foregoing acids and anhydrides, and combinations thereof. Preferably, the polyhydroxy compound of the third moiety is selected from the group consisting of glycerol, sorbitol, hydroxyquinone, glucose, mannose, 6-carbon sugars, pentose, fructose, 5-carbon sugars, pentaerythritol, catechol, resorcinol, hydroquinone, pyrogallol, 4,4'-dihydroxybiphenyl, 2,4- dihydroxybiphenyl, 2,2'-dihydroxybiphenyl, orthohydroxybenzene, polyhydroxyaromatic compounds having one or two phenyl rings and one or two 5-6 membered aromatic rings having substituted alkyl or alkenyl side chains (C 2- ι 0 ) substituted with at least two hydroxyl groups, trimethylolpropane, pentaerythritol, dimethylolpropane, dipentaerythritol, trimethylolethane, ethyleneglycol, polypropyleneglycol, polyethylated alcohols, and combinations thereof. Preferably, the polyamino compound is selected from the group consisting of diethylenetriamine, dimefhylenetriamme, dipropylnetriamine, ethyenediamine, propylenediamine, butylenediamine, butylenetriamine, triethylenetetramine, tripropylenetetramine, trimethylenetriamine, tributylenetetramine, tetraethylenepentamine, tetramethylenepentamine, tetrapropylenepentamine, tetraethylenepentamine, tetrabutylenepentamine, hexylenediamine, and combinations thereof. Preferably, the first reaction is conducted under continuous mixing. Preferably, the esterification reaction comprises reaction conditions of from about 150 °C to about 190 °C under an inert atmosphere and further comprises adding an esterification catalyst. Most preferably, the esterification catalyst is an acid catalyst. Most preferably, the esterification catalyst is selected from the group consisting of p-toluene sulfonic acid, hydrophosphorous acid, sulfuric acid, hydrochloric acid, phosphoric acid, acid-activated clays, solid acid catalysts, acidic zeolites, and combinations thereof. Preferably, the amidification reaction comprises reaction conditions of from about 130 °C to about 150 °C under an inert atmosphere. The present invention provides a diesel fuel composition having a fuel lubricity additive compound, comprising a diesel fuel and from about 50 ppm to about 5000 ppm of a fuel lubricity additive, wherein the fuel lubricity additive comprises an intermediate adduct of a first moiety reacted in a first reaction with a second moiety to form the intermediate adduct and further esterifying or amidifying the intermediate adduct with a third moiety in a molar ratio of from about 1 :2 to about 2:1, wherein the first moiety is a unsaturated triglyceride plant oil or a telomerized polymer thereof, wherein the second moiety is a diene or conjugated carbon- carbon double bond acid or anhydride moiety, wherein the first reaction comprises mixing the first moiety with the second moiety in a molar ratio of from about 1 :2 to about 2:1 at a temperature of from about 130 °C to about 195 °C under an inert atmosphere; and wherein the third moiety is a polyhydroxy compound. Preferably, the unsaturated plant oil is selected from the group consisting of rapeseed oil. tung oil, linseed oil, soya oil, corn oil, peanut oil, canola oil, safflower oil, or combinations thereof Preferably, the thermal polymer is selected from the group consisting of thermal (telomer) polymers of canola oil, soya oil, linseed oil, corn oil, safflower oil, peanut oil, tung oil, and combinations thereof Preferably, the second moiety compπses unsaturated compounds having a free carboxylic acid or anhydπde group Most preferably, the second moiety is selected from the group consisting of maleic acid, maleic anhydπde, sorbic acid, sorbic anhydπde, tetrahydrophthalic anhydπde, tetrahydrophthalic acid, salicylic acid, salicylic anhydπde, acrylic acid, acrylic anhydπde, Ci 1 0 alkyl, C 2 1 0 alkenyl, or Ci 1 0 alkoxy deπvatives of the foregoing acids and anhydndes, and combinations thereof Preferably, the polyhydroxy compound of the third moiety is selected from the group consisting of glycerol, sorbitol, hydroxyquinone, glucose, mannose, 6-carbon sugars, pentose, fructose, 5-carbon sugars, pentaerythπtol, orthohydroxybenzene, polyhydroxyaromatic compounds having one or two phenvl rings and at least two hydroxyl groups (e g , having a phenyl moiety substituted in anv of the foregoing polyhydroxy compounds), tπmethylolpropane, polyethoxylated alcohols, and combinations thereof Preferably, the polyamino compound is selected from the group consisting of diethylenetπamine, dimethylenetπamine, dipropylnetπamme, ethyenediamme, propylenediamine, butylenediamme, butylenetπamme, tπethylenetetramme, tπpropylenetetramme, tπmethylenetπamme, tπbutylenetetramine, tetraethylenepentamine, tetramethylenepentamine, tetrapropylenepentamine, tetraethylenepentamine, tetrabutylenepentamine, hexylenediamme, and combinations thereof Preferably, the first reaction is conducted under continuous mixing Preferably, the esteπfication reaction compπses reaction conditions of from about 150 °C to about 190 °C under an inert atmosphere and further compπses adding an esteπfication catalyst Most preferably, the esteπfication catalyst is an acid catalyst Most preferably, the esteπfication catalyst is selected from the group consisting of p-toluene sulfonic acid, hydrophosphorous acid, sulfuπc acid, hydrochloπc acid, phosphoπc acid, acid-activated clays, solid acid catalysts, acidic zeolites, and combinations thereof Most preferably, the fuel lubπcity additive compound is made from the first moiety, second moiety and third moiety compounds selected from the group consisting of in order soya oil-maleic anhydπde-sorbitol, soya oil-linseed oil combmation-maleic anhydπde-sorbitol, soya oil-maleic anhydπde- ethylenediamine, and soya oil-maleic anhydπde-hydroqumone A fuel lubπcity additive or a dispersant compπsmg the product of a first and a second reaction, (a) wherein the first reaction is an adduction reaction of a base oil and a dienophile having a carboxylic acid moiety selected from a formula I or a formula III // R - C = CH- O - R 3 I wherein R, R] and R 2 are independently hydrogen, hydroxyl, a straight chain or branched chain 3 - l -12 alkyl, Ci .12 acyl, Ci .12 ar l, C4.12 cycloalkyl, or Cι_i2 alkoxy; and wherein R is hydrogen, a straight chain or branched chain C _ι 2 alkyl, Ci _12 acyl, Ci .12 aryl, C4..12 cycloalkyl, or Ci .12 alkoxy, or formula II 0 R 2 Ri I I - C - C = C - R I I or formula III C = C / \ 0 = C C = 0 I II \ 0 wherein Ri and R 2 are the same as in formula I; and (b) wherein the second reaction is an esterifying or an amidafying of the carboxylic acid functional moiety of the aliphatic intermediate product of the first reaction with a polyol compound or polyamino compound having from 2 to 10 free hydroxyl groups and selected from the group consisting of substituted or unsubstituted mono-, di-, tri-, tetra- or penta-sugars, glycerols, glycols, pentaerythrols, and combinations thereof, wherein the substitutions are selected from the group consisting of hydroxyl, oxo, halogen (chloro, bromo, iodo, fluoro), straight chain or branched chain Cι _i 2 alkyl, C1..12 acyl, Ci _i2 ar Yl 4.12 cycloalkyl, hydroxyl, and Ci .12 alkoxy. Preferably, the dienoid carboxylic acid is selected from the group consisting of maleic acid, sorbic acid, acrylic acid, and combinations thereof. Preferably, the base oil is selected from the group consisting of HEAR (high erucic acid rapeseed oil), linseed oil, soybean oil, canola oil, telomer oil having a kinematic viscosity of 6000 SUS, and combinations thereof. Preferably, wherein the base oil is either a triglyceride (all straight chain) with at least one of the acyl chains being unsaturated, or a straight chain wax ester of from about 18-48 carbons atoms in length and being at least monounsaturated. Most preferably, the base oil acyl fatty acid chains of the triglyceride are from 3 to 24 carbon atoms in length (straight) and have from one to three double bonds. Most preferably, the base oil unsaturated fatty acid acyl chains have from 10-24 carbons atoms. Brief Description of the Figures Figure 1 shows a chemical structure of the product of a reaction between an unsaturated fatty acid and a dienoid adduct and then further esterification or amidification. Specifically, the structure shown in Figure 1 is the reaction product, according to the present invention, of HEAR (high erucic acid rapeseed oil), maleic anhydride and trimethylolpropane. Figure 2 shows the results of a 4 ball wear test of rapeseed oil as the base oil, maleic anhydride or sorbic acid as a carboxylic acid-containing adduct and sorbitol or glycerine as the esterified polyol. These data shown are for low viscosity polyalphaolefin (POA, a synthetic paraffinic oil with no sulfur), which can serve as an extreme model of hydrotreated diesel oil. Moreover, addition of the inventive additive (5% by weight) provided significant antiwear properties to PAO as measured by decreased wear scar size. Figure 3A shows improvement in SLBOCLE loads with increasing concentrations of HEAR-sorbic acid-sorbitol and soy oil-sorbic acid-sorbitol additives at the concentrations noted. Figure 3B shows improvement in HFRR scars with increasing concentration of the same additives. Detailed Description of the Invention Synthetic Process The synthetic process for the production of the inventive dispersants or fuel lubricity additives is a two-step process. The first step reacts the triglyceride with a dieneophile in a Diels-Alder reaction. This first step is an adduction reaction accomplished by reacting an unsaturated site of an unsaturated triglyceride oil, such as HEAR, with a dieneophile having conjugation of the double bonds and carboxylic acid group. Examples of the dieneoids are maleic anhydride, acrylic acid, sorbic acid, and ascorbic acid (vitamin C). All of the adducts are characterized by having a conjugated double bond moiety that is not sterically hindered for the Diels-Alder reaction and a free carboxylic acid moiety available for reaction in the second process step. The Diels-Alder reaction is initiated, for example, by mixing the unsaturated triglyceride and the dieneophile on a 1 :1 molar basis and adding a small amount (0.5% to 5% by weight of the dienophile)of di-t-butylperoxide and heat (range of 120 °C to 180 °C). The Diels Alder reaction proceeded until there was no further evolution of vapor phase of water, butanol (from the catalyst di-t-butylperoxide) and unreacted adduct component. The results of the first reaction step using HEAR as the unsaturated triglyceride and either styrene, maleic anhydride, acrylic acid or sorbic acid at various molar ratios is provided in Table 1. Table 1 dieneophile molar ratio exotherm, acid number iodine % complete copolymer:H max delta, number (calculated) EAR °C maleic 0.5:1 9 24.6 74.7 100 anhydride maleic 1:1 24 65.9 58.7 85 anhydride acrylic acid 1:1 liquid 100 66.3 100 addition sorbic acid 1:1 <5 32.0 95.0 62 The second step reacts the carboxylic acid moiety on an aliphatic ring intermediate with either a polyol or polyamine polar reactant (in a esterification or amidification reaction, depending upon the reactant) to form final products that are dispersants or diesel fuel lubricity additives. Illustrative polyols include glycerol (three hydroxyl groups) and the sugar derivative sorbitol with six chiral hydroxyl groups. Illustrative polyamines included ethylenediamine (EDA) having two amine moieties and tetraethylene pentamine having five amine groups. The second reaction step was carried out in the presence of hypophosphorous acid (and could also include, for example, solid acids such as silica gel, alumina or acid-activated clays, or combinations thereof) and an optional esterification catalyst (preferably at the lower reaction temperatures) at a temperature within the range of from about 150 °C to about 230 °C. Compounds The inventive fuel lubricity additives or dispersants can be illustrated according to formula IV. wherein R] is an unsaturated plant oil; wherein R 2 is independently a branched or unbranched, substituted or unsubstituted Cι- 2 o alkyl or a C 2 . 2 o alkenyl group wherein a double bond (if present) is located at least six carbon atoms away from a ring carbon atom and wherein a substitution is selected from the group consisting of hydroxyl, oxo, keto, amino, aminyl, carboxyl, amidinyl, phenyl, and tolueneyl; and wherein R 3 is a polyhydroxy third group moiety. Example 1 This example summarizes the data presented herein. Intermediate products with a number of dienes and dienoids with HEAR oil as the exemplary base oil were synthesized to form the resultant intermediate product in three molar ratios The optimum molar ratio was chosen by testing of the viscosity, viscosity index (VI), acid number, iodine number, solubility, 4-ball wear properties The molar ratios chosen from these tests were HEAR:maleιc anhvdπde @ 1:0.5, HEAR acrylic acid @ 1.1, and HEAR sorbic acid @ 1 0.6. The anti-wear properties of the sorbic acid/HEAR were the best of the above-noted intermediate products, improving the polyalphaolefin (PAO) base stock by 30% All the intermediate products were soluble in the three base stocks up to at least 5%. The intermediate products were further reacted with polar compounds to produce candidate polyol and polyamine products. The intermediate products were esteπfied with polyols glyceπne (three hydroxyls), and sorbitol (six hydroxyls) They were also reacted with ethylenediamine (EDA) and tetraethylene pentamine (TEPA) to form polyamines The polyols and polyamines were tested for anti-wear properties They were evaluated for solubihtv in base stocks and for emulsibihty in water as a condition of detergency The liquids (polyol esters) and waxes (polyamine amides) that were made were veπfied by Fouπer Transform Infrared (FTIR) Spectrophotometry for chemical structure 11 the requisite structures for the expected products were present The solubility of the products was altered drastically depending on the polar compound added Polyamines displayed the lowest solubility problems in all base stocks The sorbitol esters were the only polyols that had problems dissolving, and then, only, in PAO A level of 0 2% of the candidate compounds in MVI 100N was emulsified 50 50 with water and allowed to separate None of the glycenne esters had an effect on the oil/water separation The sorbitol esters formed stable water-in-oil emulsions and are candidates for a anti-wear dispersant/detergent compound The polyamine waxes had solubility problems with oil and produced unstable emulsions Example 2 This provides a summary of nine compositions made showing each or the tree mateπals, molar ratios and reaction conditions to illustrate the extent and breadth of the invention The following Table 5 summanzes these reactions and data. Table 5 "HPA=Hypophosphorus Acid Example 3 This provides a summary of data evaluating various diesel fuel lubricity additives for lubricity, fuel properties, combustion and deposits. Lubricity was measured using an industry standard Scuffing Load Ball on Cylinder (SLBOCLE), ASTM D-6078, and High Frequency Reciprocating Rig (HFRR), ASTM D-6079 tests. The data compare no lubricity additive with three different concentrations of inventive lubricity additive SSS-1.7.7, which is a soy oil- sorbic acid-sorbitol product at 1 : 1 molar ratios. The data are provided in Table 6. Table 6 In addition, the fuel properties of a diesel fuel containing 500 ppm of the inventive SSS-1.7.7 fuel lubricity additive showed that the fuel properties were not affected by addition of 500 ppm of the inventive fuel lubricity additive. Table 7 TEST REFERENCE 500 ppm SSS 1.7.7 ADDED An emissions and combustion test was conducted on a 276 CID, John Deere 4276T turbocharged, direct-injected, 4 cylinder diesel engine mounted on a dynomometer The engine speed and torque output were vaπed in three sections duπng the 125 hour test Any problems with combustion or injector deposits show up as high final values of Hydrocarbons and Carbon Monoxide (CO) and smoke (BSN) in the exhaust The diesel fuel used had 500 ppm of SSS-1 7 7 added The data provided m Table 8 show that the fuel with additive did not affect any change m engine operation Table 8 The values are within expeπmental error for each of the initial and final readings, indicating little or no change in the engine operation A Cummins L- 10 deposits test was run with a Cummms 6 cylinder diesel engine in accordance with Cummms Test Method 60032 The fuel used was Howell 0 4% (4000 ppm) Sulfur fuel, the only reference fuel available for the method (Cummins has not chosen a low- sulfur reference fuel as of this study ) The results of the Cummms L-10 deposit test in Table 9 show that the inventive diesel fuel lubπcity additive did not affect the deposit characteπstics of the fuel to any significant degree Table 9

Claims: We claim: 1. A fuel lubricity additive compound, comprising an intermediate adduct of a first moiety reacted in a first reaction with a second moiety to form the intermediate adduct and further esterifying or amidifying the intermediate adduct with a third moiety in a molar ratio of from about 1 :2 to about 2: 1, wherein the first moiety is a unsaturated triglyceride plant oil or a thermal polymer thereof, wherein the second moiety is a diene or conjugated double bond acid or anhydride moiety, wherein the first reaction comprises mixing the first moiety with the second moiety in a molar ratio of from about 1 :2 to about 2: 1 at a temperature of from about 130 °C to about 195 °C under an inert atmosphere; and wherein the third moiety is a polyhydroxy compound or a polyamino compound. 2. The fuel lubricity additive of claim 1 wherein the unsaturated plant oil is selected from the group consisting of rapeseed oil, tung oil, linseed oil, soya oil, corn oil, peanut oil, canola oil, safflower oil, or combinations thereof. 3. The fuel lubricity additive of claim 1 wherein the thermal polymer is selected from the group consisting of thermal (telomer) polymers of canola oil, soya oil, linseed oil, corn oil, safflower oil, peanut oil, tung oil, and combinations thereof. 4. The fuel lubricity additive of claim 1 wherein the second moiety comprises unsaturated compounds having a free carboxylic acid or anhydride group. 5. The fuel lubricity additive of claim 4 wherein the second moiety is selected from the group consisting of maleic acid, maleic anhydride, sorbic acid, sorbic anhydride, tetrahydrophthalic anhydride, tetrahydrophthalic acid, salicylic acid, salicylic anhydride, acrylic acid, acrylic anhydride, C MO alkyl, C 2 _ιo alkenyl, or Ci-io alkoxy derivatives of the foregoing acids and anhydrides, and combinations thereof. 6. The fuel lubricity additive of claim 1 wherein the polyhydroxy compound of the third moiety is selected from the group consisting of glycerol, sorbitol, hydroxyquinone, glucose, mannose, 6-carbon sugars, pentose, fructose, 5-carbon sugars, pentaerythritol, catechol, resorcinol, hydroquinone, pyrogallol, 4,4'-dihydroxybiphenyl, 2,4- dihydroxybiphenyl, 2,2'-dihydroxybiphenyl, orthohydroxybenzene, polyhydroxyaromatic compounds having one or two phenyl rings and one or two 5-6 membered aromatic rings having substituted alkyl or alkenyl side chains (C 2- ιo) substituted with at least two hydroxyl groups, trimethylolpropane, pentaerythritol, dimethylolpropane, dipentaerythritol, trimethylolethane, ethyleneglycol, polypropyleneglycol, polyethylated alcohols, and combinations thereof. 7. The fuel lubricity additive of claim 1 wherein the polyamino compound is selected from the group consisting of diethylenetriamine, dimethylenetriamine, dipropylenetriamine, ethyenediamine, propylenediamine, butylenediamine, butylenetriamine, triethylenetetramine, tripropylenetetramine, trimethylenetriamine, tributylenetetramine, tetraethylenepentamine, tetramefhylenepentamine, tetrapropylenepentamine, tetrabutylenepentamine, hexylenediamine, and combinations thereof. 8. The fuel lubricity additive of claim 1 wherein the first reaction is conducted under continuous mixing. 9. The fuel lubricity additive of claim 1 wherein the esterification reaction comprises reaction conditions of from about 150 °C to about 190 °C under an inert atmosphere and further comprises adding an esterification catalyst. 10. The fuel lubricity additive of claim 9 wherein the esterification catalyst is an acid catalyst. 11. The fuel lubricity additive of claim 10 wherein the esterification catalyst is selected from the group consisting of p-toluene sulfonic acid, hydrophosphorous acid, sulfuric acid, hydrochloric acid, phosphoric acid, acid-activated clays, solid acid catalysts, acidic zeolites, and combinations thereof. 12. The fuel lubricity additive of claim 1 wherein the amidification reaction comprises reaction conditions of from about 130 °C to about 150 °C under an inert atmosphere. 13. The fuel lubricity additive of claim 1 wherein the fuel lubricity additive compound is made from the first moiety, second moiety and third moiety compounds selected from the group consisting of in order soya oil-maleic anhydride-sorbitol, soya oil-linseed oil combination-maleic anhydride-sorbitol, soya oil-maleic anhydride-ethylenediamine, and soya oil-maleic anhydride-hydroquinone. 14. A process for synthesizing a fuel lubricity additive compound, comprising (a) reacting an unsaturated triglyceride plant oil or a thermal polymer thereof first moiety with a second moiety in a molar ratio of from about 1 :2 to about 2:1 at a temperature of from about 130 °C to about 195 °C under an inert atmosphere to form an intermediate adduct, wherein the second moiety is a diene or conjugated double bond acid or anhydride moiety; and (b) esterifying or amidifying the intermediate adduct with a third moiety in a molar ratio of from about 1 :2 to about 2:1, wherein the third moiety is a polyhydroxy compound or a polyamino compound. 15. The process of claim 14 wherein the unsaturated plant oil is selected from the group consisting of rapeseed oil, tung oil, linseed oil, soya oil, corn oil, peanut oil, canola oil, safflower oil, or combinations thereof. 16. The process of claim 14 wherein the thermal polymer is selected from the group consisting of thermal (telomer) polymers of canola oil, soya oil, linseed oil, corn oil, safflower oil, peanut oil, tung oil, and combinations thereof. 17. The process of claim 14 wherein the second moiety comprises unsaturated compounds having a free carboxylic acid or anhydride group. 18. The process of claim 17 wherein , the second moiety is selected from the group consisting of maleic acid, maleic anhydride, sorbic acid, sorbic anhydride, tetrahydrophthalic anhydride, tetrahydrophthalic acid, salicylic acid, salicylic anhydride, acrylic acid, acrylic anhydride, Ci-io alkyl, C 2- ιo alkenyl, or Cι. 10 alkoxy derivatives of the foregoing acids and anhydrides, and combinations thereof. 19. The process of claim 14 wherein the polyhydroxy compound of the third moiety is selected from the group consisting of glycerol, sorbitol, hydroxyquinone, glucose, mannose, 6-carbon sugars, pentose, fructose, 5-carbon sugars, pentaerythritol, catechol, resorcinol, hydroquinone, pyrogallol, 4,4'-dihydroxybiphenyl, 2,4-dihydroxybiphenyl, 2,2'- dihydroxybiphenyl, orthohydroxybenzene, polyhydroxyaromatic compounds having one or two phenyl rings and one or two 5-6 membered aromatic rings having substituted alkyl or alkenyl side chains (C 2-I Q) substituted with at least two hydroxyl groups, trimethylolpropane, pentaerythritol, dimethylolpropane, dipentaerythritol, trimethylolethane, ethyleneglycol, polypropyleneglycol, polyethylated alcohols, and combinations thereof. 20. The process of claim 14 wherein the polyamino compound is selected from the group consisting of diethylenetriamine, dimethylenetriamine, dipropylnetriamine, ethyenediamine, propylenediamine, butylenediamine, butylenetriamme, triethylenetetramine, tripropylenetetramine, trim ethylenetri amine, tributylenetetramine, tetraethylenepentamine, tetramethylenepentamine, tetrapropylenepentamine, tetraethylenepentamine, tetrabutylenepentamine, hexylenediamine, and combinations thereof. 21. The process of claim 14 wherein the first reaction is conducted under continuous mixing. 22. The process of claim 14 wherein the esterification reaction comprises reaction conditions of from about 150 °C to about 190 °C under an inert atmosphere and further comprises adding an esterification catalyst. 23. The process of claim 14 wherein the esterification catalyst is an acid catalyst. 24. The process of claim 23 wherein the esterification catalyst is selected from the group consisting of p-toluene sulfonic acid, hydrophosphorous acid, sulfuric acid, hydrochloric acid, phosphoric acid, acid-activated clays, solid acid catalysts, acidic zeolites, and combinations thereof. 25. The process of claim 14 wherein the amidification reaction comprises reaction conditions of from about 130 °C to about 150 °C under an inert atmosphere. 26. A fuel lubricity additive or a dispersant comprising a product of a first and a second reaction, (a) wherein the first reaction is an adduction reaction of a base oil and a dienophile having a carboxylic acid moiety selected from a formula I or a formula III: R - C = C-C- O - R 3 I wherein R, Ri and R 2 are independently hydrogen, hydroxyl, a straight chain or branched chain C}_12 alkyl, Cι_i2 acyl, Ci _ι 2 aryl, C4.12 cycloalkyl, or Ci _γ alkoxy; and wherein R 3 is hydrogen, a straight chain or branched chain Cj.i 2 alkyl, Ci .12 acyl, Ci .12 aryl, C4. 2 cycloalkyl, or C \_\2 alkoxy, or formula II 0 R 2 R x ,/ I I - C - C = C - R I I or formula III I I C = C / \ 0 = c c = 0 i n \ / o wherein Ri and R 2 are the same as in formula I, and (b) wherein the second reaction is an esteπfying or an amidafying of the carboxylic acid functional moiety of the aliphatic intermediate product of the first reaction with a polyol compound or polyamino compound having from 2 to 10 free hydroxyl groups and selected from the group consisting of substituted or unsubstituted mono-, di-, tn-, tetra- or penta-sugars, glycerols, glycols. pentaerythrols, and combinations thereof, wherein the substitutions are selected from the group consisting of hydroxyl, oxo, halogen (chloro, bromo, lodo, fluoro), straight chain or branched chain C1. 2 a lkyl C] _i2 ac yl > Ci _12 ar yl> 4.12 cycloalkyl, hydroxyl, and C1.12 alkoxy 27 The fuel lubπcity additive of claim 26, wherein the dienoid carboxylic acid is selected from the group consisting of maleic acid, phtha c acid, sorbic acid, acrylic acid, and combinations thereof 28 The fuel lubπcity additive of claim 26, wherein the base oil is selected from the group consisting of HEAR (high erucic acid rapeseed oil), lmseed oil, soybean oil, canola oil, telomer oil having a kinematic viscosity of 6000 SUS, and combinations thereof 29 The fuel lubπcity additive of claim 26, wherein the base oil is either a tπglyceπde (all straight chain) with at least one of the acyl chains being unsaturated, or a straight chain wax ester of from about 18-48 carbons atoms in length and being at least monounsaturated 30 The fuel lubπcity additive of claim 29, wherein the base oil acyl fatty acid chains of the tπglyceπde are from 3 to 24 carbon atoms in length (straight) and have from one to three double bonds 31 The fuel lubπcity additive of claim 30, wherein the base oil unsaturated fatty acid acyl chains have from 10-24 carbons atoms

Inventors: LANDIS PHILLIP S, RHODES BLAINE N, WILLIAMSON WILL F, LANDIS, PHILLIP, S., RHODES, BLAINE, N., WILLIAMSON, WILL, F.
Applicants: INT LUBRICANTS INC, INTERNATIONAL LUBRICANTS, INC.
Application year: 1999
Main classification: C10L1
IPC codes: C07C69, C10L1, C10L10