Acylated nitrogen compounds useful as additives for lubricating oil and fuel compositions

Abstract: A process for reacting certain carboxylic reactants with olefinic compounds then reacting the product prepared thereby with ammonia, a hydrazine or an amine, products prepared thereby and, additive concentrates, lubricating oil and fuel compositions.

Description: This invention relates to acylated nitrogen compounds which are useful as low chlorine containing additives for lubricating oils and normally liquid fuels and a process for preparing the compounds. Background of the Invention Numerous types of additives are used to improve lubricating oil and fuel compositions. Such additives include, but are certainly not limited to dispersants and detergents of the ashless and ash-containing variety, oxidation inhibitors, anti-wear additives, friction modifiers, and the like. Such materials are well known in the art and are described in many publications, for example, Smalheer, et al, "Lubricant Additives", Lezius-Hiles Co., Cleveland, OH, USA (1967); M.W. Ranney, Ed., "Lubricant Additives", Noyes Data Corp., Park Ridge, NJ, USA (1973); M.J. Satriana, Ed., "Synthetic Oils and Lubricant Additives, Advances since 1977", Noyes Data Corp., Park Ridge NJ, USA (1982), W.C. Gergel, "Lubricant Additive Chemistry", Publication 694-320-65R1 of the Lubrizol Corp., Wickliffe, OH, USA (1994); and W.C. Gergel et al, "Lubrication Theory and Practice" Publication 794-320-59R3 of the Lubrizol Corp., Wickliffe, OH, USA (1994); and in numerous United States patents, for example Chamberlin, III, US 4,326,972, Schroeck et al, US 4,904,401, and Ripple et al, US 4,981,602. Many such additives are frequently derived from carboxylic reactants, for example, acids, esters, anhydrides, lactones, and others. Specific examples of commonly used carboxylic compounds used as intermediates for preparing lubricating oil additives include alkyl-and alkenyl substituted succinic acids and anhydrides, polyolefin substituted carboxylic acids, aromatic acids, such as salicylic acids, and others. Illustrative carboxylic compounds are described in Meinhardt, et al, US 4,234,435; Norman et al, US 3,172,872; LeSuer et al, US 3,454,607, and Rense, US 3,215,707. Many carboxylic intermediates used in the preparation of lubricating oil additives contain chlorine. While the amount of chlorine present is often only a very small amount of the total weight of the intermediate, the chlorine frequently is carried over into the carboxylic derivative which is desired as an additive. For a variety of reasons, including environmental reasons, the industry has been making efforts to reduce or to eliminate chlorine from additives designed for use as lubricant or fuel additives. The matter of chlorine content in additives is discussed in numerous patents including U.S. patent nos. 5, 356,552; 5,370,805; 5,445,657 and 5,454,964. Accordingly, it is desirable to provide low chlorine or chlorine free additives for use in lubricants and fuels. The present invention provides acylated nitrogen compounds which meet this requirement. B.B. Snider and J.W. van Straten, J. Org. Chem., 44, 3567-3571 (1979) describe certain products prepared by the reaction of methyl glyoxylate with several butenes and cyclohexenes. K. Mikami and M. Shimizu, Chem. Rev., 92, 1021-1050 (1992) describe carbonyl-ene reactions, including glyoxylate-ene reactions. D. Savostianov (communicated by P.Pascal), C.R. Acad. Sc. Paris, 263, (605-7) (1966) relates to preparation of some α-hydroxylactones via the action of glyoxylic acid on olefins. M. Kerfanto et. al., C.R. Acad. Sc. Paris, 264, (232-5) (1967) relates to condensation reactions of α-α-di-(N-morpholino)-acetic acid and glyoxylic acid with olefins. B.B. Jarvis et al, Synthesis, 1079-82 (1990) relates to reactions of oxocarboxylic acids with olefins under acidic conditions to give α-hydroxy butyrolactones. DE-A-2103686 describes a process for the preparation of α-hydroxy-γ-lactones by the reaction of an α-oxocarboxylic acid with an olefinicly unsaturated compound at a temperature of 50 to 240°C in the presence of a weak acid catalyst having a pKa at 25°C of 1 to 6. EP-A-0624638 describes the reaction of a substituted phenol with an oxocarboxylic acid to form an intermediate compound which is subsequently reacted with an amine. Fuels containing additives to improve the performance thereof are described in the numerous patents including the following United States patents: 4,071,327 5,336,278 4,379,065 5,356,546 4,400,178 5,458,793 4,564,460 Summary of the Invention The present invention provides a process comprising first reacting, optionally in the presence of an acidic catalyst selected from the group consisting of organic sulfonic acids, heteropolyacids, Lewis acids, and mineral acids, (A) at least one olefinic compound containing at least one group of the formula and (B) at least one carboxylic reactant selected from the group consisting of compounds of the formula R 3 C(O)(R 4 ) n C(O)OR 5 (IV) and compounds of the formula wherein each of R 3 , R 5 and R 9 is independently H or a hydrocarbyl group, R 4 is a divalent hydrocarbylene group, and n is 0 or 1; wherein (A) and (B) are reacted in amounts ranging from more than 1.5 moles (B) per mole of (A) to 3 moles (B) per equivalent of (A); then reacting the product formed thereby with from 0.5 equivalents up to 2 moles, per mole of (B) of at least one of (C) ammonia or a hydrazine or an amine characterized by the presence within its structure of at least one H―N group; and products prepared by this process. Also provided are additive concentrates for preparing lubricating oil and fuel compositions, lubricating oil compositions and fuel compositions. Various preferred features and embodiments of the invention are hereinafter described by way of non-limiting illustration. As used herein, the terms "hydrocarbon", "hydrocarbyl" or "hydrocarbon based" mean that the group being described has predominantly hydrocarbon character within the context of this invention. These include groups that are purely hydrocarbon in nature, that is, they contain only carbon and hydrogen. They may also include groups containing non-hydrocarbon substituents or atoms which do not alter the predominantly hydrocarbon character of the group. Such substituents may include halo-, alkoxy-, nitro-, etc. These groups also may contain hetero atoms. Suitable hetero atoms will be apparent to those skilled in the art and include, for example, sulfur, nitrogen and oxygen. Therefore, while remaining predominantly hydrocarbon in character within the context of this invention, these groups may contain atoms other than carbon present in a chain or ring otherwise composed of carbon atoms. In general, no more than about three non-hydrocarbon substituents or hetero atoms, and preferably no more than one, will be present for every 10 carbon atoms in the hydrocarbon, hydrocarbyl or hydrocarbon based groups. Most preferably, the groups are purely hydrocarbon in nature, that is they are essentially free of atoms other than carbon and hydrogen. Throughout the specification and claims the expression soluble or dispersible is used. By soluble or dispersible is meant that an amount needed to provide the desired level of activity or performance can be incorporated by being dissolved, dispersed or suspended in an oil of lubricating viscosity or in a normally liquid fuel. Usually, this means that at least 0.001 % by weight of the material can be incorporated in a lubricating oil or normally liquid fuel. For a further discussion of the terms oil soluble and dispersible, particularly "stably dispersible", see US Patent 4,320,019. As noted hereinabove, provided by this invention are certain acylated nitrogen compounds and a process for preparing low chlorine or chlorine free compositions useful as low chlorine or chlorine free additives for lubricating oil and fuel compositions. The Process In another embodiment, the present invention relates to a process comprising first reacting, optionally in the presence of an acidic catalyst selected from the group consisting of organic sulfonic acids, heteropolyacids, Lewis acids, and mineral acids, (A) at least one olefinic compound containing at least one group of the formula and (B) at least one carboxylic reactant selected from the group consisting of compounds of the formula R 3 C(O)(R 4 ) n C(O)OR 5 (IV) and compounds of the formula wherein each of R 3 , R 5 and R 9 is independently H or a hydrocarbyl group, R 4 is a divalent hydrocarbylene group, and n is 0 or 1; wherein (A) and (B) are reacted in amounts ranging from more than 1.5 moles (B) per mole of (A) to 3 moles (B) per equivalent of (A); then reacting the product formed thereby with from 0.5 equivalents up to 2 moles, per mole of (B) of at least one of (C) ammonia or a hydrazine or an amine characterized by the presence within its structure of at least one H―N group. The first step of the process may be conducted in the presence of an azeotroping solvent. Well known azeotroping solvents include toluene, xylene, cyclohexane, etc. Cyclohexane is preferred. The Catalyst The first step of the process of this invention is optionally conducted in the presence of an acidic catalyst. Acid catalysts, such as organic sulfonic acids, for example, paratoluene sulfonic acid, methane sulfonic acid and sulfonated polymers such as those marketed under the tradename Amberlyst® (Rohm & Haas), heteropolyacids, the complex acids of heavy metals (e.g., Mo, W, Sn, V, Zr, etc.) with phosphoric acids (e.g., phosphomolybdic acid), and mineral acids, for example, H 2 SO 4 and phosphoric acid, are useful. The amount of catalyst used is generally small, ranging from 0.01 mole % to 10 mole %, more often from 0.1 mole % to 2 mole %, based on moles of olefinic reactant. (A) The Olefinic Compound The olefinic compound employed as a reactant in the process of this invention contains at least one group of the formula and has the general formula (R 1 )(R 2 )C=C(R 6 )(CH(R 7 )(R 8 )) wherein each of R 1 and R 2 is, independently, hydrogen or a hydrocarbon based group. Each of R 6 , R 7 and R 8 is, independently, hydrogen or a hydrocarbon based group; preferably at least one is a hydrocarbon based group containing at least 7 carbon atoms. These olefinic compounds are diverse in nature. Virtually any compound containing an olefinic bond may be used provided it meets the general requirements set forth hereinabove for (III) and does not contain any functional groups (e.g., primary or secondary amines) that would interfere with the carboxylic reactant (B). Useful olefinic compounds may be terminal olefins, i.e., olefins having a H 2 C=C group, or internal olefins. Useful olefinic compounds may have more than one olefinic bond, i.e., they may be dienes, trienes, etc. Most often they are mono-olefinic. Examples include linear ∝-olefins, cis- or trans- disubstituted olefins, trisubstituted olefins and tetrasubstituted olefins. When (A) is a monoolefinic, one mole of (A) contains one equivalent of C=C; when (A) is diolefinic, one mole of (A) contains 2 equivalents of C=C bonds; when (A) is triolefinic, one mole of (A) contains 3 equivalents of C=C bonds, and so forth. Aromatic double bonds are not considered to be olefinic double bonds within the context of this invention. As used herein, the expression "polyolefin" defines a polymer derived from olefins. The expression "polyolefinic" refers to a compound containing more than one C=C bond. Among useful compounds are those that are purely hydrocarbon, i.e., those substantially free of non-hydrocarbon groups, or they may contain one or more non-hydrocarbon groups as discussed in greater detail herein. In one embodiment, the olefinic compounds are substantially hydrocarbon, that is, each R group in (III) is H or contains essentially carbon and hydrogen. In one aspect within this embodiment, each of R 1 , R 2 , R 7 and R 8 is hydrogen and R 6 is a hydrocarbyl group containing from 7 to 5,000 carbon atoms, more often from 30 up to 200 carbon atoms, preferably from 50 up to 100 carbon atoms. In another aspect of this embodiment, each of R 1 and R 2 is hydrogen, R 6 is H or a lower alkyl group and the group (CH(R 7 )(R 8 )) is a hydrocarbyl group containing from 7 to 5,000 carbon atoms, more typically from 30 up to 200 carbon atom, preferably from 50 up to 100 carbon atoms. In another embodiment, one or more of the R groups present in (III) is an organic radical which is not purely hydrocarbon. Such groups may contain or may be groups such as carboxylic acid, ester, amide, salt, including ammonium, amine and metal salts, cyano, hydroxy, thiol, tertiary amino, nitro, alkali metal mercapto and the like. Illustrative of olefinic compounds (III) containing such groups are methyl oleate, oleic acid, 2-dodecenedioic acid, octene diol, linoleic acid and esters thereof, and the like. Preferably, the hydrocarbyl groups are aliphatic groups. In one preferred embodiment, when an R group is an aliphatic group containing a total of from 30 to 100 carbon atoms, the olefinic compound is derived from homopolymerized and interpolymerized C 2-18 mono- and di-olefins, preferably 1- olefins. In a preferred embodiment, the olefins contain from 2 to 5 carbon atoms, preferably 3 or 4 carbon atoms. Examples of such olefins are ethylene, propylene, butene-1, isobutylene, butadiene, isoprene, 1-hexene, 1-octene, etc. R groups can, however, be derived from other sources, such as monomeric high molecular weight alkenes (e.g. 1-tetracontene), aliphatic petroleum fractions, particularly paraffin waxes and cracked analogs thereof, white oils, synthetic alkenes such as those produced by the Ziegler-Natta process (e.g., poly-(ethylene) greases) and other sources known to those skilled in the art. Any unsaturation in the R groups may be reduced by hydrogenation according to procedures known in the art, provided at least one olefinic group remains as described for (III). In one preferred embodiment, at least one R is derived from polybutene, that is, polymers of C 4 olefins, including 1-butene, 2-butene and isobutylene. Those derived from isobutylene, i.e., polyisobutylenes, are especially preferred. In another preferred embodiment, R is derived from polypropylene. In another preferred embodiment, R is derived from ethylene-alpha olefin polymers, including ethylene-propylene-diene polymers. Representative of such polymers are the ethylene-propylene copolymers and ethylene-propylene-diene terpolymers marketed under the Trilene® tradename by the Uniroyal Company. Molecular weights of such polymers may vary over a wide range, but especially preferred are those having number average molecular weights ( M n ) ranging from 300 to 20,000, preferably 700 to 10,000, often from 900 to 2,500. In one preferred embodiment, the olefin is an ethylene-propylene-diene terpolymer having M n ranging from 900 to 8,000, often up to 2,000. Such materials are included among the Trilene® polymers marketed by the Uniroyal Company, Middlebury, CT, USA and Ortholeum® 2052 marketed by the DuPont Company. Ethylene-alpha olefin copolymers and ethylene-lower olefin-diene terpolymers are described in numerous patent documents, including European patent publication EP 279,863, Japanese patent publication 87-129,303 and the following United States patents: 3,598,738 4,357,250 4,026,809 4,658,078 4,032,700 4,668,834 4,137,185 4,937,299 4,156,061 5,324,800 4,320,019 A preferred source of hydrocarbyl groups R are polybutenes obtained by polymerization of a C 4 refinery stream having a butene content of 35 to 75 weight percent and isobutylene content of 15 to 60 weight percent in the presence of a Lewis acid catalyst such as aluminum trichloride or boron trifluoride. These polybutenes contain predominantly (greater than 80% of total repeating units) isobutylene repeating units of the configuration These polybutenes are typically monoolefinic, that is they contain but one olefinic bond per molecule. The olefinic compound may be a polyolefin comprising a mixture of isomers wherein from 50 percent to 65 percent are tri-substituted olefins wherein one substituent contains from 2 to 500 carbon atoms, often from 30 to 200 carbon atoms, more often from 50 to 100 carbon atoms, usually aliphatic carbon atoms, and the other two substituents are lower alkyl. When the olefin is a tri-substituted olefin, it frequently comprises a mixture of cis- and trans- 1-lower alkyl, 1-(aliphatic hydrocarbyl containing from 30 to 100 carbon atoms), 2-lower alkyl ethene and 1,1-di-lower alkyl, 2-(aliphatic hydrocarbyl containing from 30 to 100 carbon atoms) ethene. In one embodiment, the monoolefinic groups are predominantly vinylidene groups, i.e., groups of the formula especially those of the formula although the polybutenes may also comprise other olefinic configurations. In one embodiment the polybutene is substantially monoolefinic, comprising at least 30 mole %, preferably at least 50 mole % vinylidene groups, more often at least 70 mole % vinylidene groups. Such materials and methods for preparing them are described in U.S. Patents 5,071,919; 5,137,978; 5,137,980; 5,286,823 and 5,408,018, and in published European patent application EP646103-A1. They are commercially available, for example under the tradenames Ultravis® (BP Chemicals) and Glissopal® (BASF). As is apparent from the foregoing, olefins of a wide variety of type and of molecular weight are useful for preparing the compositions of this invention. Useful olefins are usually substantially hydrocarbon and have number average molecular weight ranging from 100 to 70,000, more often from 200 to 7,000, even more often from 1,300 to 5,000, frequently from 400 to 3,000. Specific characterization of olefin reactants (A) used in the processes of this invention can be accomplished by using techniques known to those skilled in the art. These techniques include general qualitative analysis by infrared and determinations of average molecular weight, e.g. M n , number average molecular weight, and M w , weight average molecular weight, etc. employing vapor phase osmometry (VPO) and gel permeation chromatography (GPC). Structural details can be elucidated employing proton and carbon 13 (C 13 ) nuclear magnetic resonance (NMR) techniques. NMR is useful for determining substitution characteristics about olefinic bonds, and provides some details regarding the nature of the substituents. More specific details regarding substituents about the olefinic bonds can be obtained by cleaving the substituents from the olefin by, for example, ozonolysis, then analyzing the cleaved products, also by NMR, GPC, VPO, and by infra-red analysis and other techniques known to the skilled person. (B) The Carboxylic Reactant The carboxylic reactant is at least one member selected from the group consisting of compounds of the formula R 3 C(O)(R 4 ) n C(O)OR 5 (IV) and compounds of the formula wherein each of R 3 , R 5 and R 9 is independently H or a hydrocarbyl group. R 3 is usually H or an aliphatic group, that is, alkyl or alkenyl, preferably alkyl, more preferably lower alkyl. Especially preferred is where R 3 is H or methyl, most preferably, H. R 4 is a divalent hydrocarbylene group. This group may be aliphatic or aromatic, but is usually aliphatic. Often, R 4 is an alkylene group containing from 1 to 3 carbon atoms. The 'n' is 0 or 1; that is, in one embodiment R 4 is present and in another embodiment, R 4 is absent. More often, R 4 is absent. When R 5 is hydrocarbyl, it is usually an aliphatic group, often a group containing from 1 to 30 carbon atoms, often from 8 to 18 carbon atoms. In another embodiment, R 5 is lower alkyl, wherein "lower alkyl" is defined hereinabove. Most often, R 5 is H or lower alkyl. R 9 is H or hydrocarbyl, preferably H or lower alkyl. Examples of carboxylic reactants (B) are glyoxylic acid, and other omega-oxoalkanoic acids, keto alkanoic acids such as pyruvic acid, levulinic acid, ketovaleric acids, ketobutyric acids and numerous others. The skilled worker, having the disclosure before him, will readily recognize the appropriate compound of formula (V) to employ as a reactant to generate a given compound. Reactant (B) may be a compound of the formula wherein each of R 3 and R 5 is independently H or alkyl. Such compounds arise when the carbonyl reactant is hydrated. Glyoxylic acid monohydrate is a representative example. The intermediate arising from the reaction of (A) and (B) may be a carboxylic acid or a lactone. Often, the intermediate arising from the reaction of (A) and (B) is a mixture comprising both lactone and carboxylic acid. (C) Ammonia, Hydrazine and Amine Reactants Suitable (C) reactants, as defined herein, include ammonia, hydrazines, monoamines or polyamines. The (C) reactants must contain at least one N-H group. The monoamines generally contain from 1 to 24 carbon atoms, preferably 1 to 12, and more preferably 1 to 6. Examples of monoamines useful in the present invention include primary amines, for example methylamine, ethylamine, propylamine, butylamine, octylamine, and dodecylamine. Examples of secondary amines include dimethylamine, diethylamine, dipropylamine, dibutylamine, methylbutylamine, ethylhexylamine, etc. Tertiary monoamines will not result in formation of an amide, but can form salts with carboxylic acids. In another embodiment, the monoamine may be a hydroxyamine. Typically, the hydroxyamines are primary or secondary alkanolamines or mixtures thereof. As stated above, tertiary monoamines will not react to form amides; however tertiary alkanol monoamines sometimes can react to form a tertiary amino group containing ester. Alkanol amines that can react to form amide can be represented, for example, by the formulae: H 2 N―R'―OH, and wherein each R 4 is independently a hydrocarbyl group of one to 22 carbon atoms or hydroxyhydrocarbyl group of two to 22 carbon atoms, preferably one to four, and R' is a divalent hydrocarbyl group of two to 18 carbon atoms, preferably two to four. The group -R'-OH in such formulae represents the hydroxyhydrocarbyl group. R' can be an acyclic, alicyclic or aromatic group. Typically, R' is an acyclic straight or branched alkylene group such as an ethylene, 1,2-propylene, 1,2-butylene, 1,2-octadecylene, etc. group. When two R 4 groups are present in the same molecule they can be joined by a direct carbon-to-carbon bond or through a heteroatom (e.g., oxygen, nitrogen or sulfur) to form a 5-, 6-, 7- or 8-membered ring structure. Examples of such heterocyclic amines include N-(hydroxyl lower alkyl)-morpholines, -thiomorpholines, -piperidines, -oxazolidines, -thiazolidines and the like. Typically, however, each R 4 is independently a methyl, ethyl, propyl, butyl, pentyl or hexyl group. Examples of these alkanolamines include mono-, di-, and triethanolamine, diethylethanolamine, ethylethanolamine, butyldiethanolamine, etc. The hydroxyamines can also be ether N-(hydroxyhydrocarbyl) amines. These are hydroxy poly(hydrocarbyloxy) analogs of the above-described hydroxy amines (these analogs also include hydroxyl-substituted oxyalkylene analogs). Such N-(hydroxyhydrocarbyl) amines can be conveniently prepared, for example, by reaction of epoxides with aforedescribed amines and can be represented by the formulae: H 2 N ― (R'O) x ― H, and wherein x is a number from 2 to 15 and R 4 and R' are as described above. R 4 may also be a hydroxypoly (hydrocarbyloxy) group. Other useful amines include ether amines of the general formula R 6 OR 1 NHR 7 wherein R 6 is a hydrocarbyl group, preferably an aliphatic group, more preferably an alkyl group, containing from 1 to 24 carbon atoms, R 1 is a divalent hydrocarbyl group, preferably an alkylene group, containing from two to 18 carbon atoms, more preferably two to 4 carbon atoms and R 7 is H or hydrocarbyl, preferably H or aliphatic, more preferably H or alkyl, more preferably H. When R 7 is not H, then it preferably is alkyl containing from one to 24 carbon atoms. Especially preferred ether amines are those available under the name SURFAM® produced and marketed by Sea Land Chemical Co., Westlake, Ohio. The amine may also be a polyamine. The polyamine may be aliphatic, cycloaliphatic, heterocyclic or aromatic. Examples of the polyamines include alkylene polyamines, hydroxy containing polyamines, arylpolyamines, and heterocyclic polyamines. Alkylene polyamines are represented by the formula wherein n has an average value between 1 and 10, preferably 2 to 7, more preferably 2 to 5, and the "Alkylene" group has from 1 to 10 carbon atoms, preferably 2 to 6, more preferably 2 to 4. R 5 is independently hydrogen or an aliphatic or hydroxy-substituted aliphatic group of up to 30 carbon atoms. Preferably R 5 is H or lower alkyl, most preferably, H. Alkylene polyamines include methylene polyamines, ethylene polyamines, butylene polyamines, propylene polyamines, pentylene polyamines, etc. Higher homologs and related heterocyclic amines such as piperazines and N-amino alkylsubstituted piperazines are also included. Specific examples of such polyamines are ethylene diamine, diethylene triamine, triethylene tetramine, tris-(2-aminoethyl)amine, propylene diamine, trimethylene diamine, tripropylene tetramine, tetraethylene pentamine, hexaethylene heptamine, pentaethylenehexamine, aminoethyl piperazine, dimethyl aminopropylamine, etc. Higher homologs obtained by condensing two or more of the above-noted alkylene amines are similarly useful as are mixtures of two or more of the aforedescribed polyamines. Ethylene polyamines, such as some of those mentioned above, are preferred. They are described in detail under the heading Ethylene Amines in Kirk Othmer's "Encyclopedia of Chemical Technology", 2d Edition, Vol. 7, pages 22-37, Interscience Publishers, New York (1965). Such polyamines are most conveniently prepared by the reaction of ethylene dichloride with ammonia or by reaction of an ethylene imine with a ring opening reagent such as water, ammonia, etc. These reactions result in the production of a complex mixture of polyalkylene polyamines including cyclic condensation products such as the aforedescribed piperazines. Ethylene polyamine mixtures are useful. Other useful types of polyamine mixtures are those resulting from stripping of the above-described polyamine mixtures to leave as residue what is often termed "polyamine bottoms". In general, alkylene polyamine bottoms can be characterized as having less than two, usually less than 1% (by weight) material boiling below 200°C. A typical sample of such ethylene polyamine bottoms obtained from the Dow Chemical Company of Freeport, Texas, designated "E-100"® has a specific gravity at 15.6°C of 1.0168, a percent nitrogen by weight of 33.15 and a viscosity at 40°C of 1.21 x 10 -4 m 2 .s -1 (121 centistokes). Gas chromatography analysis of such a sample contains about 0.93% "Light Ends" (most probably diethylenetriamine), 0.72% triethylenetetramine, 21.74% tetraethylene pentaamine and 76.61% pentaethylene hexamine and higher (by weight). These alkylene polyamine bottoms include cyclic condensation products such as piperazine and higher analogs of diethylenetriamine, triethylenetetramine and the like. Another useful polyamine is a condensation product obtained by reaction of at least one hydroxy compound with at least one polyamine reactant containing at least one primary or secondary amino group. The hydroxy compounds are preferably polyhydric alcohols and amines. Preferably the hydroxy compounds are polyhydric amines. Polyhydric amines include any of the above-described monoamines reacted with an alkylene oxide (e.g., ethylene oxide, propylene oxide, butylene oxide, etc.) having two to 20 carbon atoms, preferably two to four. Examples of polyhydric amines include tri-(hydroxypropyl)amine, tris-(hydroxymethyl)amino methane, 2-amino-2-methyl-1,3-propanediol, N,N,N',N'-tetrakis(2-hydroxypropyl) ethylenediamine, and N,N,N',N'-tetrakis(2-hydroxyethyl) ethylenediamine. Polyamine reactants, which react with the polyhydric alcohol or amine to form the condensation products or condensed amines, are described above. Preferred polyamine reactants include triethylenetetramine (TETA), tetraethylenepentamine (TEPA), pentaethylenehexamine (PEHA), and mixtures of polyamines such as the above-described "amine bottoms". The condensation reaction of the polyamine reactant with the hydroxy compound is conducted at an elevated temperature, usually 60°C to 265°C in the presence of an acid catalyst. The amine condensates and methods of making the same are described in Steckel (US 5,053,152). In another embodiment, the polyamines are hydroxy-containing polyamines. Hydroxy-containing polyamine analogs of hydroxy monoamines, particularly alkoxylated alkylenepolyamines can also be used. Such polyamines can be made by reacting the above-described alkylene amines with one or more of the above-described alkylene oxides. Similar alkylene oxide-alkanolamine reaction products can also be used such as the products made by reacting the aforedescribed primary, secondary or tertiary alkanolamines with ethylene, propylene or higher epoxides in a 1.1 to 1.2 molar ratio. Reactant ratios and temperatures for carrying out such reactions are known to those skilled in the art. Specific examples of alkoxylated alkylenepolyamines include N-(2-hydroxyethyl) ethylenediamine, N,N-di-(2-hydroxyethyl)-ethylenediamine, 1-(2-hydroxyethyl) piperazine, mono-(hydroxypropyl)-substituted tetraethylenepentamine, N-(3-hydroxybutyl)-tetramethylene diamine, etc. Higher homologs obtained by condensation of the above illustrated hydroxy-containing polyamines through amino groups or through hydroxy groups are likewise useful. Condensation through amino groups results in a higher amine accompanied by removal of ammonia while condensation through the hydroxy groups results in products containing ether linkages accompanied by removal of water. Mixtures of two or more of any of the aforesaid polyamines are also useful. In another embodiment, the polyamine may be a heterocyclic polyamine. The heterocyclic polyamines include aziridines, azetidines, azolidines, tetra- and dihydropyridines, pyrroles, indoles, piperidines, imidazoles, di- and tetrahydroimidazoles, piperazines, isoindoles, purines, N-aminoalkylmorpholines, N-aminoalkylthiomorpholines, N-aminoalkylpiperazines, N,N'-bisaminoalkyl piperazines, azepines, azocines, azonines, azecines and tetra-, di- and perhydro derivatives of each of the above and mixtures of two or more of these heterocyclic amines. Preferred heterocyclic amines are the saturated 5- and 6-membered heterocyclic amines containing only nitrogen, or nitrogen with oxygen and/or sulfur in the hetero ring, especially the piperidines, piperazines, thiomorpholines, morpholines, pyrrolidines, and the like. Piperidine, aminoalkylsubstituted piperidines, piperazine, aminoalkylsubstituted piperazines, morpholine, aminoalkylsubstituted morpholines, pyrrolidine, and aminoalkyl-substituted pyrrolidines, are especially preferred. Usually the aminoalkyl substituents are substituted on a nitrogen atom forming part of the hetero ring. Specific examples of such heterocyclic amines include N-aminopropylmorpholine, N-aminoethylpiperazine, and N,N'-diaminoethyl-piperazine. Hydroxy alkyl substituted heterocyclic polyamines are also useful. Examples include N-hydroxyethylpiperazine and the like. In another embodiment, the amine is a polyalkene-substituted amine. These polyalkene-substituted amines are well known to those skilled in the art. They are disclosed in U.S. patents 3,275,554; 3,438,757; 3,454,555; 3,565,804; 3,755,433; and 3,822,289. Typically, polyalkene-substituted amines are prepared by reacting halogenated-, preferably chlorinated-, olefins and olefin polymers (polyalkenes) with amines (mono- or polyamines). The amines may be any of the amines described above. Examples of these compounds include poly(propylene)amine; N,N-dimethyl-N-poly (ethylene/propylene)amine, (50:50 mole ratio of monomers); polybutene amine; N,N-di(hydroxyethyl)-N-polybutene amine; N-(2-hydroxypropyl)-N-polybutene amine;N-polybutene-aniline; N-polybutenemorpholine; N-poly(butene) ethylenediamine; N-poly(propylene)trimethylenediamine; N-poly(butene)diethylene-triamine; N',N'-poly(butene)tetraethylenepentamine; N,N-dimethyl-N'-poly-(propylene)-1,3-propylenediamine and the like. The polyalkene substituted amine is characterized as containing from at least 8 carbon atoms, preferably at least 30, more preferably at least 35 up to 300 carbon atoms, preferably 200, more preferably 100. In one embodiment, the polyalkene substituted amine is characterized by an n (number average molecular weight) value of at least 500. Generally, the polyalkene substituted amine is characterized by an n value of 500 to 5000, preferably 800 to 2500. In another embodiment n varies between 500 to 1200 or 1300. The polyalkenes from which the polyalkene substituted amines are derived include homopolymers and interpolymers of polymerizable olefin monomers of 2 to 16 carbon atoms; usually 2 to 6, preferably 2 to 4, more preferably 4. The olefins may be monoolefins such as ethylene, propylene, 1-butene, isobutene, and 1-octene; or a polyolefinic monomer, preferably diolefinic monomer, such 1,3-butadiene and isoprene. Preferably, the polymer is a homopolymer. An example of a preferred homopolymer is a polybutene, preferably a polybutene in which about 50% of the polymer is derived from isobutylene. The polyalkenes are prepared by conventional procedures. It is generally preferred to utilize sufficient amine reactant (C) to convert substantially all of the intermediate arising from reaction of (A) with (B) to product; however, conversion of at least 50%, more preferably 75% is often acceptable. Preferably, at least 90%, more preferably 99-100% conversion is effected. The reaction with the (C) reactant to prepare the products of this invention is conducted at temperatures ranging from 25°C to 230°C,. When the amine is an alkanolamine, an alkylene polyamine or a thioalkanol amine, N-containing heterocyclic group containing products such as imidazoline, oxazoline, or thiazoline formation may form. These are frequently obtained by first preparing an amide then continuing the reaction at elevated temperature to generate imidazoline, thiazoline or oxazoline by removal of water. Imidazoline formation will not occur with every amine; the amine must have the structural element: H 2 NCRCR-NH-R f Similarly, oxazoline formation can take place when the amine is a β-hydroxyethyl amine, e.g., HO-CR f 2 CR f 2 -NH 2 β-thiolamines can react to form thiazolines. In the above formulae, each R f is independently H, alkoxyalkyl, hydroxyalkyl, hydrocarbyl, aminohydrocarbyl or N-alkoxyalkyl- or hydroxyalkyl- substituted amino hydrocarbyl. Thus, if imidazoline, thiazoline or oxazoline formation is not desired, they may be avoided by employing amine reactants that do not provide the opportunity for imidazoline, thiazoline or oxazoline formation, or, if the amine employed can lead to oxazoline, thiazoline or imidazoline, to minimize formation thereof by conducting the reaction at the lowest temperature to prepare amide at an acceptable rate and in acceptable amounts, or to avoid prolonged heating of the amide-containing product, once it has formed. Infrared analysis during the reaction is a convenient means for determining the nature and extent of the reaction. The first step of the process of this invention is conducted, usually under an inert atmosphere such as N 2 , at temperatures ranging from ambient up to the lowest decomposition temperature of any of the reactants, usually from 60°C to 220°C, more often from 120°C to 180°C, preferably up to 160°C. The process employs from more than 1.5 moles (B) per mole of (A) to 3 moles (B) per equivalent of (A), more often from 1.8 moles (B) per mole of (A) to 2.5 moles (B) per equivalent of (A), even more often from 1.9 moles (B) per mole of (A) to 2.1 moles (B) per equivalent of (A). The product formed in this first step is then reacted, at temperatures ranging from 25°C to 230°C, preferably from 60°C to 150°C, more often from 100°C to 110°C with (C) ammonia, a hydrazine or an amine characterized by the presence within its structure of at least one N-H group. Reactant (C) is used in amounts ranging from 0.5 equivalents up to 2 moles, per mole of (B). Products obtained by post-treating the acylated nitrogen compounds of this invention are also useful. Reagents such as urea, thiourea, carbon disulfide, aldehydes, ketones, carboxylic acids, hydrocarbon substituted succinic anhydrides, nitriles, epoxides, boron compounds, phosphorus compounds and the like are useful post-treating agents. The following examples are intended to illustrate several compositions of this invention as well as means for preparing same. Unless indicated otherwise all parts are parts by weight, filtrations are conducted employing a diatomaceous earth filter aid, and analytical values are by actual analysis. Aromatic hydrocarbons are commercial aromatic hydrocarbon solvents having a flash point of about 43°C. It is to be understood that these examples are intended to illustrate several compositions and procedures of the invention and are not intended to limit the scope of the invention. Example 1 Part A A reactor is charged with 450 parts of polyisobutene having M n about 1000 and 92 parts 50% aqueous glyoxylic acid. The materials are heated under N 2 at 200°C to 205° for 36 hours while collecting 35 parts distillate in a Dean-Stark trap. The materials are stripped to 180°C at 2 mm Hg pressure for 1 hour, then are filtered at 150°C with a diatomaceous earth filter aid. Infrared spectrum shows prominent C=O absorption. saponification No. =36. Total acid No. = 5.5 Part B A reactor is charged with 132 parts of the product of Part A, above, 15 parts of an ethylene polyamine mixture containing an average of 34% N and 90 parts mineral oil. The materials are heated, under N 2 , at 175-180°C for 48 hours, collecting 3 parts distillate in a Dean-Stark trap and filtered at 150°C. The filtrate contains 1.55%N. Infra red shows weak lactone and medium amide C=0. Example 2 Part A A reactor is charged with 1360 parts polyisobutene (Glissopal® ES3250) having M n about 1000 and containing about 87 mole percent terminal vinylidene groups, 250 parts glyoxylic acid monohydrate and 1.35 parts 70% aqueous methane sulfonic acid. The materials are heated under N 2 for 4 hours at 155°-160°C while collecting 82 parts aqueous distillate in a Dean-Stark trap. The materials are filtered at 155°-160°C with a diatomaceous earth filter aid. Infra red spectrum: very strong lactone C=O at 1774 cm -1 . Saponification No. = 107; Total acid no = 31.8, 9% unreacted polyisobutene (TLC-FID). Part B A reactor is charged with 251 parts of the product of Part A of this example and 49.7 parts of aminoethylethanolamine. The materials are heated, under N 2 , to 200°C and are held at 200°C for 3 hours, collecting 7.1 parts aqueous distillate in a Dean-Stark trap. The temperature is increased to 225°C and the material are held at temperature for 3.5 hours while collecting 2.8 parts aqueous distillate, then held at temperature for 2 more hours, collecting 0.9 parts aqueous distillate. The temperature is reduced to 150°C and the materials are maintained at temperature for 1 hour followed by addition of 94 parts aromatic hydrocarbon solvent and filtration at 120°C. % N = 2.21. Example 3 A reactor is charged with 250 parts of a product prepared as in Example 2, Part A, and 61.4 parts aminoethylpiperazine. The materials are heated, under N 2 , to 180°C and are held at temperature for 7 hours followed by heating to 200°C and heating at temperature for 5.5 hours. An additional 3.1 parts aminoethylpiperazine is added, the temperature is increased to 210°C and the materials are heated at temperature for 2 hours, cooled to 115°C and stripped at 115°C at 1 millimeter Hg pressure, collecting 3.9 parts distillate. The materials are dissolved in 103.5 parts aromatic solvent and are filtered at 120°C. Filtrate contains 4.33% N. Example 4 A reactor is charged with 215.7 parts of a product prepared as in Example 2, Part A and 32.7 parts of an ethylene polyamine mixture continuing about 25% by weight diethylenetriamine and containing 34% N. The materials are heated, under N 2 at 190°C for 4.5 hour collecting 5.3 parts distillate. The materials are cooled to 120°C, mixed with 82.8 parts mineral oil diluent and filtered. The filtrate contains 3.22% N and 1% free amine. Example 5 Part A A reactor is charged with 2300 parts of the polyisobutene of Example 2, Part A, 2.3 parts 70% aqueous methane sulfonic acid, and 680.8 parts 50% aqueous glyoxylic acid. The materials are heated under N 2 at 155-160°C for 4.5 hours, removing 390 parts aqueous distillate. Upon addition of 866 parts mineral oil diluent the materials cool to 130°C and are filtered. Part B A reactor is charged with 332 parts of the product of Part A of this example and 28.4 parts of the ethylene polyamine mixture of Example 4 with exotherm to 45°C followed by heating to 160°C then maintaining temperature for 3.5 hours while collecting 1.5 parts aqueous distillate. Heating is continued for 2 more hours while 3.1 parts additional distillate are collected. The materials are cooled to 120°C, diluted with 93.4 parts mineral oil diluent and filtered. The filtrate contains 1.93% N. Example 6 A reactor is charged with 29.9 parts of the polyamine of example 4 and 107.5 parts mineral oil then heated to 160°C To the oil solution are added 350 parts of the product of Example 5, Part A, dropwise, over 1.5 hours while maintaining 160°C. After addition is completed, the materials are heated at 160°C for 3 hours, cooled to 130° and filtered. The filtrate contains 1.86% N. Example 7 A reactor is charged with 250 parts of the product of Example 5, Part A, 28 parts of a branched polyamine derived from the condensation of tris-hydroxymethyl aminomethane with an ethylene polyamine, and 135.5 parts mineral oil diluent. The materials are heated at 160°C for 6 hours, collecting 2.1 parts aqueous distillate, then are filtered at 125°C. The filtrate contains 1.79% N. Example 8 A solution of 18 parts of oil and 18 parts of the amine used in Example 7 is heated to 160°C. To this solution are added, dropwise over 0.7 hours, 160 parts of the product of Part A of Example 5 followed by heating at 160°C for 4 hours, then filtration at 140°C. The filtrate contains 2.51% N. Example 9 To a reactor are charged 200 parts of the product of Part A of Example 5 and 17.5 parts ethylenediamine. The materials are heated at 115°C for 4 hours while collecting 1.2 parts aqueous distillate then at 160°C for 1.5 hours collecting 3.7 parts aqueous distillate. The materials are stripped to 120°C at 17 mm Hg pressure and are filtered at 120°C. The filtrate contains 1.59% N. Example 10 The procedure of example 9 is repeated employing 34.9 parts ethylene diamine. A total of 10.1 parts aqueous distillate is obtained. Example 11 A mixture of 200 parts of the product of Part A of Example 5 and 34.8 parts ethanolamine is reacted at 165°C for 6 hours under N 2 , then the materials are stripped to 120°C at 15 mm Hg and filtered. The filtrate contains 1.24%N. Example 12 A mixture of 200 parts of the product of Part A of Example 5 and 70.4 parts tris-hydroxymethyl aminomethane is reacted at 185°C for 4.5 hours removing 2.8 parts aqueous distillate. Heating is continued for 5 more hours while 12.4 parts additional aqueous distillate are collected, followed by filtration at 120°C. The filtrate contains 1.15% N. Example 13 A mixture of 250 parts of the product of Part A of Example 5 and 52.5 parts of 30% aqueous ammonia are reacted at 140°C for 2 hours while collecting 32.3 parts aqueous distillate, then the materials are stripped to 120°C at 15 mm Hg and filtered at 120°C. The filtrate contains 0.30% N. Example 14 A mixture of 250 parts of the product of Part A of Example 5 and 49.4 parts of diethylenetriamine are reacted at 160°C under for 5 hours, stripped to 100-130°C at 25 mm Hg, diluted residue with 99.8 parts aromatic solvent and filtered . The filtrate contains 2.85% N. Example 15 Part A A reactor charged with 296 parts 50% aqueous glyoxylic acid is heated to 80°C at 25 mm Hg, removing 109 parts water. The dried material is cooled to room temperature then 1000 parts of the polyisobutene of Example 2, Part A and 1.5 parts 70% aqueous methane sulfonic acid are added. The materials are heated for 5 hours at 150°C, collecting 178 parts water. The materials are filtered at 140°C. The filtrate has saponification no. = 90.8 and contains 9.1% unreacted polyisobutylene (TLC-FID). Part B A reactor is charged with 830 parts of the product of Part A of this example and 132.7 parts aminoethyl ethanolamine.. The materials are reacted at 210°C for a total of 10 hours cooled to 180°C and stripped to 190°C at 30 mm Hg. The materials are cooled to 140°C whereupon 320.9 parts aromatic solvent are added, the materials are mixed and the solution is filtered. The filtrate contains 2.86% N and 0% free amine. Example 16 Part A A reactor charged with 592 parts 50% aqueous glyoxylic acid is heated to 70°C, a vacuum is applied and the materials are stripped to 80°C at 25 mm Hg., collecting 231 parts water. The reactor is cooled to room temperature whereupon 200 parts of the polyisobutene of Example 2, Part A and 3 parts 70% aqueous methane sulfonic acid are added followed by heating for a total of 8 hours at 160°C while collecting 207 parts aqueous distillate. The materials are diluted with 717.3 parts mineral oil, mixed and filtered at 130°C. The filtrate has saponification no. = 65.9. Part B A reactor is charged with 350 parts of the product of Part A of this example, 26.6 parts of polyamine bottoms having an equivalent weight of 40.5 per N (HPA-X® , Union Carbide) and 105.3 parts mineral oil. The materials are heated, under N 2 , to 160°C and are held at temperature for 5 hours, cooled to 145°C and filtered. The filtrate contains 1.77% N. Example 17 The procedure of Example 16, Part B is repeated employing 400 parts of the product of Example 16, Part A, 30.45 parts of HPA-X® amine and 120.4 parts mineral oil. The filtrate contains 1.76% N. Example 18 A reactor is charged with 350 parts of the product of Part A of Example 16, 26 parts of an ethylene polyamine mixture (about 15% diethylene triamine, 21% tetraethylene pentamine and 64% pentaethylene hexamine; 36%N) and 104.8 parts mineral oil. The materials are heated under N 2 , for 6 hours at 160°C, cooled to 145°C and filtered. The filtrate contains 1.84% N. Example 19 A reactor is charged with 138.1 parts of the amine of Example 7 and 367.1 parts mineral oil. The amine is heated to 160°C whereupon are added 1100 parts of the product of Part A of Example 16 over 1 hour, maintaining 160°C. The materials are reacted for 5 hours at 160°C, cooled to room temperature and diluted with 367.1 parts mineral oil, heated to 140°C and filtered. The filtrate contains 2.28% N. Example 20 To a reactor are charged 400 parts of the product of Part A of Example 16, 34.92 parts 40% aqueous methylamine and 23.2 parts mineral oil. The mixture is heated, under N 2 , at 55°C for 7 hours, temperature is increased to 65°C and is held at temperature for 4 hours then 0.1 parts by volume silicone antifoam are added. The materials are heated to 120°C and held at temperature for 3 hours then temperature is increased further and materials are heated at 160°C for 5 hours. Water is collected during reaction. The materials are stripped to 160°C at 30 mm Hg and filtered. The filtrate contains 0.59% N. Example 21 Part A A reactor is charged with 3000 parts of polyisobutylene having a number average molecular weight of about 2400 and containing about 70% terminal vinylidene groups (Glissopal® ES 3252, BASF), 230.3 parts glyoxylic acid monohydrate, 17.5 parts 70% aqueous methane sulfonic acid and a few drops of a silicone antifoam agent. The materials are heated under N 2 purge (0.3 cubic feet per hour) to 130°C and then are heated at 130°C for a total of 11 hours while collecting a total of 140 parts aqueous distillate. The materials are cooled to room temperature, 2093 parts mineral oil diluent are added and the solution is stirred while heating to 130°C whereupon the solution is filtered. Saponification no. = 20.2; Total acid no. = 6.7. Unreacted polyisobutylene = 11% (TLC-FID). Part B A reactor is charged with 380 parts of the product of Part A of this example, 7.33 parts of an ethylene polyamine mixture containing about 25% diethylene triamine and the balance being heavier ethylene polyamines and containing about 34% N, and 5 parts mineral oil. The materials are heated at 160°C, under N 2 , for 5 hours, cooled to 140°C and filtered. Filtrate contains 0.70% N. Example 22 To a reactor are charged 4265 parts of the product of Part A of Example 21, 112.9 parts of the polyamine of Example 16, part B, and 75.2 parts of mineral oil. The mixture is heated over 1 hour to 160°C and are held at 160°C, under N 2 , for 6 hours, cooled to 140°C and filtered. The filtrate contains 0.82% N. Example 23 Part A A reactor is charged with 4,000 parts of a polyisobutene having M n about 1,000 and containing about 80 mole % terminal vinylidene groups, 1,184 parts 50% aqueous glyoxylic acid and 4 parts 70% aqueous methane sulfonic acid. The materials are heated to 160°C over 3 hours, under N 2 while removing aqueous distillate, then the reaction is continued at 160°C for 4 hours. A total of 615 parts aqueous distillate is collected. The materials are filtered. The filtrate contains 9% unreacted polybutene and has saponification no = 92.4. Part B A reactor is charged with 1000 parts of the product of Part A of this example, 117.6 parts of the polyamine used in Example 16, Part B, and 745.1 parts mineral oil. The materials are heated to 165°C over 0.5 hour and held at temperature, under N 2 for a total of 6 hours, cooled to 140°C and filtered. The filtrate contains 2.09% N. Example 24 Part A A reactor is charged with 2498.6 parts of a polypropylene polymer having M n ≅ 860, 860 parts 50% aqueous glyoxylic acid and 2.6 parts 70% aqueous methane sulfonic acid. The materials are heated to 140°C and held at temperature for 5 hours, collecting 268 parts water; then temperature is increased to 170°C over 6 hours, collecting 267 parts additional distillate. The materials are cooled to 140°C and filtered. The filtrate has theory saponification No. = 115. Part B A reactor is charged with 250 parts of the product of Part A of this example, 20.4 parts of the polyamine mixture used in Part B of example 21 and 178.3 parts mineral oil. The materials are heated at 160°C for 3.5 hours, collecting 1.5 parts water, then the temperature is increased to 180°C and is held at temperature for 3 hours while collecting 0.8 parts distillate. The temperature is then increased to 190°C and reaction is held at temperature for 5.5 hours, collecting 0.6 parts distillate. The reaction is cooled to 120°C, 178.3 parts mineral oil is added and the solution is filtered. Filtrate contains 1.15% N. Example 25 A mixture of 275 parts of the product of Part A of Example 24 and 33.9 parts of the polyamine mixture used in Part B of Example 21 is reacted at 160°C, under N 2 for 6 hours, collecting 2.2 parts water. The materials are mixed with 195.7 parts mineral oil and filtered at 125°C. Example 26 A reactor is charged with 250 parts of the product of Part A of Example 24 and 76 parts 30% aqueous ammonia, heated, under N 2 , to 140°C over 1.5 hours and held at temperature for 3 hours while collecting 48.6 parts water. The temperature is increased and the reaction is continued at 160°C for 2 hour, then the materials are stripped to 120°C at 20 mm Hg and filtered. The filtrate contains 0.47% N. Example 27 The product of Part A of Example 24 (250 parts) and 53.5 parts aminoethyl ethanolamine are reacted for 5.5 hours at 180°C while collecting 6.7 parts water. The reaction was then continued for 4 hours at 200°C, removing 0.9 parts distillate. The materials are stripped to 145°C at 1.5 mm Hg, collecting 9.7 parts distillate, diluted with 98.1 parts aromatic solvent, then filtered. The filtrate contains 1.0% N. Example 28 A reactor is charged with 250 parts of the product of Part A of Example 24 and 65,8 parts of aminoethylpiperazine. The materials are heated at 190° C, under N 2 , for 7 hours, then at 210°C for 5.5 hours. Aromatic diluent (105 parts) is added at 60°C, mixed and filtered. The filtrate contains 3.02% N. Example 29 Part A A reactor is charged with 518 parts of 50% aqueous glyoxylic acid which is dried by stripping to 70°C at 25 mm Hg, collecting 179 parts of aqueous distillate. To the reactor are charged 1750 parts of an ethylene-propylene copolymer having M n of about 1000 (Uniroyal) and 2.6 parts 70% aqueous methane sulfonic acid followed by heating to 160°C and holding at temperature for a total of 6 hours, collecting aqueous distillate. The material are filtered. The filtrate has saponification no = 88.5. GPC shows 100% = 1152. TLC/FID shows 0% unreacted olefin. Part B A reactor is charged with 200 parts of the product of part A of this example and 32.2 parts dimethylaminopropyl amine. The materials are heated to 160°C and are held at temperature for 4 hours; infra-red shows residual C=O at 1775 cm -1 . The temperature is increased to 180°C and the material are held at temperature for 2 hours, then the temperature is increased to 200°C and the materials are held at temperature for 6 hours. The materials are cooled to 130° and are stripped at 130°/30 mm Hg. The residue is filtered. The filtrate contains 2.9% N Example 30 The procedure of Example 29, Part B is repeated replacing dimethylaminopropyl amine with 32.8 parts aminoethyl ethanolamine. The filtrate contains 3.38% N. Example 31 A reactor is charged with 200 parts of the product of Part A of Example 29 and 33 parts diethylene triamine. The materials are heated, under N 2 , to 160° and are held ate temperature for 3.5 hours, then the temperature is increased to 200° and the materials are held at temperature for 3 hours, cooled and stripped to 150°C at 30 mm Hg and filtered. The filtrate contains 5.02% N. Example 32 Following substantially the procedure of Example 31, 200 parts of the product of Part A of Example 29 and 41.3 parts aminoethylpiperazine are reacted for 3.5 hours at 160° and for a total of 9 hours at 200°, stripped to 130°C at 35 mm Hg and filtered. The filtrate contains 4.99% N. Example 33 A reactor is charged with 200 parts of the product of Part A of Example 29 and 18.9 parts of the ethylene polyamine mixture used in Example 21, Part B. The materials are reacted at 160°C, under N 2 , for 6 hours, cooled and filtered at 130°C. The filtrate contains 1.72% N. Example 34 A reactor is charged with 200 parts of the product of Part A of Example 29 and 46 parts aminopropyl morpholine. The materials are reacted at 160°C, under N 2 , for 12 hours, cooled, stripped to 160°C at 30 mm Hg and filtered. The filtrate contains 3.54% N. Example 35 A reactor is charged with 250 parts of the product of Part A of Example 29 and 23.6 parts of ethylenediamine. The materials are reacted at 160°C for 6 hours, stripped to 130°C at 30 mm Hg and filtered. The filtrate contains 2.03% N. Example 36 A reactor is charged with 200 parts of the product of Part A of Example 29 and 24.85 parts of the amine used in Example 7. The materials are reacted at 160°C, under N 2 , for 6 hours, diluted with 149.9 parts mineral oil and filtered at 130°C.The filtrate contains 1.75% N. Example 37 A reactor is charged with 250 parts of a product prepared essentially according to the procedure of Example 2A and 24.9 parts of dimethylaminopropylamine. The materials are reacted at 200°C, under N 2 , for 6.5 hours, cooled and stripped to 120°C at 20 mm Hg, collecting 1.7 parts distillate, diluted with 91.1 parts aromatic hydrocarbon solvent and filtered at 120°C. Filtrate contains 1.4% N. Example 38 The process of Part A of Example 1 is repeated employing 0.1 mole % AlCl 3 catalyst, filtered by the process of Part B. Example 39 The process of Part A of Example 1 is repeated employing 0.1 mole % FeCl 3 catalyst, followed by the process of Part B. Example 40 The process of Part A of Example 1 is repeated employing 0.2 mole % BF 3 catalyst, followed by the process of Part B. Example 41 The process of Example 1 is repeated replacing glyoxylic acid with an equal molar amount of pyruvic acid. Example 42 The process of Example 1 is repeated replacing glyoxylic acid with an equal molar amount of levulinic acid. Example 43 The product of Example 1, Part B is post treated with 1 % by weight H 3 BO 3 at 130°C, removing aqueous distillate as it forms. The Lubricating Oil Compositions The Oil of Lubricating Viscosity In one embodiment of this invention, the compositions are lubricating oil compositions. The lubricating compositions employ an oil of lubricating viscosity, including natural or synthetic lubricating oils and mixtures thereof. Mixtures of mineral oil and synthetic oils, particularly polyalphaolefin oils and polyester oils, are often used. Natural oils include animal oils and vegetable oils (e.g. castor oil, lard oil and other vegetable acid esters) as well as mineral lubricating oils such as liquid petroleum oils and solvent-treated or acid treated mineral lubricating oils of the paraffinic, naphthenic or mixed paraffinic-naphthenic types. Hydrotreated or hydrocracked oils are included within the scope of useful oils of lubricating viscosity. Oils of lubricating viscosity derived from coal or shale are also useful. Synthetic lubricating oils include hydrocarbon oils and halosubstituted hydrocarbon oils such as polymerized and interpolymerized olefins, etc. and mixtures thereof, alkylbenzenes, polyphenyl, (e.g., biphenyls, terphenyls, alkylated polyphenyls, etc.), alkylated diphenyl ethers and alkylated diphenyl sulfides and their derivatives, analogs and homologues thereof and the like. Alkylene oxide polymers and interpolymers and derivatives thereof, and those where terminal hydroxyl groups have been modified by esterification, etherification, etc., constitute other classes of known synthetic lubricating oils that can be used. Another suitable class of synthetic lubricating oils that can be used comprises the esters of dicarboxylic acids and those made from C 5 to C 12 monocarboxylic acids and polyols or polyol ethers. Other synthetic lubricating oils include liquid esters of phosphorus-containing acids, polymeric tetrahydrofurans and the like, silicon-based oils such as the polyalkyl-, polyaryl-, polyalkoxy-, or polyaryloxy-siloxane oils and silicate oils. Hydrotreated naphthenic oils are well known. Unrefined, refined and rerefined oils, either natural or synthetic (as well as mixtures of two or more of any of these) of the type disclosed hereinabove can used in the compositions of the present invention. Unrefined oils are those obtained directly from a natural or synthetic source without further purification treatment. Refined oils are similar to the unrefined oils except they have been further treated in one or more purification steps to improve one or more properties. Rerefined oils are obtained by processes similar to those used to obtain refined oils applied to refined oils which have been already used in service. Such rerefmed oils often are additionally processed by techniques directed to removal of spent additives and oil breakdown products. Specific examples of the above-described oils of lubricating viscosity are given in Chamberlin III, U.S. 4,326,972 and European Patent Publication 107,282. A basic, brief description of lubricant base oils appears in an article by D.V. Brock, "Lubrication Engineering", Volume 43, pages 184-5, March, 1987. Other Additives The lubricating oil compositions of this invention may contain minor amounts of other components. The use of such components is optional and the presence thereof in the compositions of this invention will depend on the particular use and level of performance required. Thus these components may be included or excluded. The compositions may comprise a zinc salt of a dithiophosphoric acid. Zinc salts of dithiophosphoric acids are often referred to as zinc dithiophosphates, zinc O,O-dihydrocarbyl dithiophosphates, and other commonly used names. They are sometimes referred to by the abbreviation ZDP. One or more zinc salts of dithiophosphoric acids may be present in a minor amount to provide additional extreme pressure, anti-wear and anti-oxidancy performance. In addition to zinc salts of dithiophosphoric acids discussed hereinabove, other additives that may optionally be used in the lubricating oils of this invention include, for example, detergents, dispersants, viscosity improvers, oxidation inhibiting agents, metal passivating agents, pour point depressing agents, extreme pressure agents, anti-wear agents, color stabilizers and anti-foam agents. The above-mentioned dispersants and viscosity improvers are used in addition to the additives of this invention. Auxiliary extreme pressure agents and corrosion and oxidation inhibiting agents which may be included in the compositions of the invention are exemplified by chlorinated aliphatic hydrocarbons, organic sulfides and polysulfides, phosphorus esters including dihydrocarbon and trihydrocarbon phosphites, molybdenum compounds, and the like. Viscosity improvers (also sometimes referred to as viscosity index improvers) may be included in the compositions of this invention. Viscosity improvers are usually polymers, including polyisobutenes, polymethacrylic acid esters, diene polymers, polyalkyl styrenes, alkenylarene-conjugated diene copolymers and polyolefins. Multifunctional viscosity improvers, other than those of the present invention, which also have dispersant and/or antioxidancy properties are known and may optionally be used in addition to the products of this invention. Such products are described in numerous publications including those mentioned in the Background of the Invention. Pour point depressants are a particularly useful type of additive often included in the lubricating oils described herein. See for example, page 8 of 'Lubricant Additives" by C.V. Smalheer and R. Kennedy Smith (Lezius-Hiles Company Publisher, Cleveland, Ohio, 1967). Pour point depressants useful for the purpose of this invention, techniques for their preparation and their use are described in U. S. Patent numbers 2,387,501; 2,015,748; 2,655,479; 1,815,022; 2,191,498; 2,666,748; 2,721,877; 2,721,878; and 3,250,715. Anti-foam agents used to reduce or prevent the formation of stable foam include silicones or organic polymers. Examples of these and additional anti-foam compositions are described in "Foam Control Agents", by Henry T. Kerner (Noyes Data Corporation, 1976), pages 125-162. Detergents and dispersants may be of the ash-producing or ashless type. The ash-producing detergents are exemplified by oil soluble neutral and basic salts of alkali or alkaline earth metals with sulfonic acids, carboxylic acids, phenols or organic phosphorus acids characterized by at least one direct carbon-to-phosphorus linkage. The term "basic salt" is used to designate metal salts wherein the metal is present in stoichiometrically larger amounts than the organic acid radical. Basic salts and techniques for preparing and using them are well known to those skilled in the art and need not be discussed in detail here. Ashless detergents and dispersants are so-called despite the fact that, depending on its constitution, the detergent or dispersant may upon combustion yield a nonvolatile residue such as boric oxide or phosphorus pentoxide; however, it does not ordinarily contain metal and therefore does not yield a metal-containing ash on combustion. Many types are known in the art, and any of them are suitable for use in the lubricants of this invention. The following are illustrative: (1) Reaction products of carboxylic acids (or derivatives thereof) containing at least 34 and preferably at least 54 carbon atoms with nitrogen containing compounds such as amine, organic hydroxy compounds such as phenols and alcohols, and/or basic inorganic materials. Examples of these "carboxylic dispersants" are described in British Patent number 1,306,529 and in many U.S. patents including the following: 3,163,603 3,381,022 3,542,680 3,184,474 3,399,141 3,567,637 3,215,707 3,415,750 3,574,101 3,219,666 3,433,744 3,576,743 3,271,310 3,444,170 3,630,904 3,272,746 3,448,048 3,632,510 3,281,357 3,448,049 3,632,511 3,306,908 3,451,933 3,697,428 3,311,558 3,454,607 3,725,441 3,316,177 3,467,668 4,194,886 3,340,281 3,501,405 4,234,435 3,341,542 3,522,179 4,491,527 3,346,493 3,541,012 RE 26,433 3,351,552 3,541,678 (2) Reaction products of relatively high molecular weight aliphatic or alicyclic halides with amines, preferably polyalkylene polyamines. These may be characterized as "amine dispersants" and examples thereof are described for example, in the following U.S. patents: 3,275,554 3,454,555 3,438,757 3,565,804 (3) Reaction products of alkyl phenols in which the alkyl groups contains at least 30 carbon atoms with aldehydes (especially formaldehyde) and amines (especially polyalkylene polyamines), which may be characterized as "Mannich dispersants". The materials described in the following U. S. patents are illustrative: 3,413,347 3,725,480 3,697,574 3,726,882 3,725,277 (4) Products obtained by post-treating the carboxylic amine or Mannich dispersants with such reagents are urea, thiourea, carbon disulfide, aldehydes, ketones, carboxylic acids, hydrocarbon-substituted succinic anhydrides, nitriles, epoxides, boron compounds, phosphorus compounds or the like. Exemplary materials of this kind are described in the following U.S. patents: 3,036,003 3,282,955 3,493,520 3,639,242 3,087,936 3,312,619 3,502,677 3,649,229 3,200,107 3,366,569 3,513,093 3,649,659 3,216,936 3,367,943 3,533,945 3,658,836 3,254,025 3,373,111 3,539,633 3,697,574 3,256,185 3,403,102 3,573,010 3,702,757 3,278,550 3,442,808 3,579,450 3,703,536 3,280,234 3,455,831 3,591,598 3,704,308 3,281,428 3,455,832 3,600,372 3,708,522 4,234,435 (5) Interpolymers of oil-solubilizing monomers such as decyl methacrylate, vinyl decyl ether and high molecular weight olefins with monomers containing polar substituents, e.g., aminoalkyl acrylates or methacrylates, acrylamides and poly(oxyethylene)-substituted acrylates. These may be characterized as "polymeric dispersants" and examples thereof are disclosed in the following U.S. patents: 3,329,658 3,666,730 3,449,250 3,687,849 3,519,565 3,702,300 The above-illustrated additives may each be present in lubricating compositions at a concentration of as little as 0.001 % by weight usually ranging from 0.01% to 20% by weight, more often from 1% to 12% by weight. The compositions of the present invention are present in a minor amounts, often amounts ranging from 1% to 20% by weight, more often from 3% to 10% by weight, even more often from 5% to 8% by weight. Additive Concentrates The various additives described herein can be added directly to the lubricating oil or fuel. Preferably, however, they are diluted with a substantially inert, normally liquid organic diluent such as mineral oil, naphtha, benzene, toluene or xylene, to form an additive concentrate. These concentrates usually comprise 0.1 to 80% by weight, frequently from 1% to 80% by weight, more often from 10% to 80% by weight, of the compositions of this invention and may contain, in addition, one or more other additives known in the art or described hereinabove. Concentrations such as 15%, 20%, 30% or 50% or higher may be employed. Additive concentrates are prepared by mixing together, often at elevated temperature, the desired components. Additive concentrates used for preparing lubricating oil compositions are illustrated by the following examples. The amounts shown are indicated as parts by weight or parts by volume. Unless indicated otherwise, components are indicated as parts or percentages by weight of chemical present on an oil or diluent free basis. When products of Examples set forth hereinabove are used, the amounts listed are so prepared, including diluent, if any. Additive concentrates are prepared by blending the components listed in the following Tables. Mineral oil is used to bring the total to 100 parts. Example: A B C Component: (parts by weight) Polybutene ( M ∼ 1300) subst. succinic anhydride-ethylene polyamine reaction product 19.5 Ca overbased (MR ∼ 1.1) S-coupled alkyl phenate 7.6 7.0 7.0 Ca overbased (MR ∼ 3.5) S-coupled alkyl phenate 1.5 Di-(nonyl phenyl) amine 1.8 2.0 2.0 Zinc salt of di-mixed isopropyl-ethylhexyl dithiophosphate 8.6 Ca overbased (MR ∼ 1.2) alkyl benzene sulfonate 3.4 3.9 3.9 Mg overbased (MR 14.7) alkyl benzene sulfonate 2.5 3.2 3.2 Silicone antifoam 0.01 0.01 0.01 Product of Example 23B 15.6 Zinc salt of di-mixed isopropyl-isoctyl dithiophosphate 9.1 8.2 Ca overbased (MR ∼ 2.3) S-coupled phenate 4.8 4.8 Product of Example 21B 34.9 Polybutene ( M n ∼ 1000) substituted succinic anhydride-pentaerythritol/alkylene amine reaction product 9.0 9.0 Product of Example 17 34.38 Example: D E F Component: (parts by weight) t-Butyl-propylene tetramer substituted phenol 2.7 2.4 5.7 Ca overbased (MR ∼ 2.3) S-coupled alkyl phenate 2.9 2.6 Zinc salt of di-mixed isopropyl-methyl amyl dithiophosphate 7.8 8.5 9.4 Sulfurized (13.9% S) Butadiene-butyl acrylate Diels-Alder adduct 4.3 3.9 di(nonyl phenyl) amine 1.9 1.7 2.2 Sunflower oil 0.9 0.8 0.9 Ca overbased (MR ∼ 1.2) alkyl benzene sulfonate 1.8 1.6 Na overbased (MR ∼ 15) polybutene M n ∼ 1000) substituted succinic acid 2.4 2.1 6.1 Mg overbased (MR ∼ 14.7) alkyl benzene sulfonate 2.4 2.2 1.5 Silicone antifoam 0.01 0.01 0.01 Polybutene M n ∼ 1000) substituted succinic anhydride-pentaerythritol-ethylene polyamine reaction product 8.9 Sulfurized (26% S) butadiene-butyl acrylate Diels-Alder adduct 5.2 Product of Example 22 54.1 Product of Example 21B 32.52 Product of Example 17 47.8 Example: G H Component: (parts by weight) Borated rctn product of polybutene ( M n ∼ 1000) subst. succinic anhydride and ethylene polyamine 2.2 Dibutyl phosphite 0.83 2.9 Styrene-maleate copolymer neutralized with aminopropyl morpholine 15.46 13.5 Hydrorefined mineral oil 8.33 21.9 Di(nonyl phenyl) amine 1.7 6.1 Dithiocarbamate from dibutyl dithiocarbamic acid and methyl acrylate 4.2 Mercaptan-propylene oxide reaction product 6.3 Product of Example 17 29.2 Product of Example 19 29.2 The lubricating compositions of this invention are illustrated in the following Examples. The lubricating compositions are prepared by combining the specified ingredients, individually or from concentrates, in the indicated amounts and oil of lubricating viscosity to make the total 100 parts by weight. The amounts shown are indicated as parts by weight or parts by volume. Unless indicated otherwise, where components are indicated as parts by weight, they are amounts of chemical present on an oil or diluent free basis. Thus, for example, an additive comprising 50% oil used at 10% by weight in a blend, provides 5% by weight of chemical.Totals are 100% by weight or 100 parts by weight. However, when referring to incorporation of products of Examples set forth herein, amounts are as prepared. Examples I - II Lubricating oil compositions are prepared by mixing together in a mineral oil of lubricating viscosity (Exxon 15W-40), 7.5 parts of a 91% oil solution of an ethylene-propylene-diene copolymer, 0.08 parts of a styrene-maleate copolymer neutralized with aminopropylmorpholine and the indicated amount of the additive concentrates set forth in the following table: Additive Concentrate/Parts by WeightU Example I Example B/12.9 II Example C/12.8 Example III Lubricating oil composition is prepared by mixing together in a mineral oil of lubricating viscosity (Exxon 15W-40), 7.5 parts of a 91% oil solution of an ethylene-propylene-diene copolymer, 0.08 parts of a styrene-maleate copolymer neutralized with aminopropyl morpholine, and the indicated amount of the additive concentrate set forth in the following table: Additive Concentrate/Parts by Weight Example III Example A/13.5 Example IV A lubricating oil composition is prepared by mixing together a mineral oil of lubricating viscosity (Exxon 5W-30), 8.5% of a commercial viscosity improver (ECA 13112, Exxon) and 11.09% of the additive concentrate of Example D. Example V A lubricating oil composition is prepared by mixing together a mineral oil of a lubricating viscosity (Valvoline 5W-30), 8.75% of a commercial viscosity improver (ECA® 13114, Exxon) and 12.3% of the additive concentrate of Example E. Example VI A lubricating oil composition is prepared by mixing together a mineral oil of lubricating viscosity (Conoco 5W-30), 1% of a styrene-diene copolymer viscosity improver and 0.08% of a styrene-maleate copolymer neutralized with aminopropyl morpholine and 11.5% of the additive concentrate of Example F. Example VII An automatic transmission fluid is prepared by mixing together in a mineral oil of lubricating viscosity, (Exxon Dexron® III Base), 0.025% of a red dye, 0.01% of a mixture of silicone antifoam agents and 12% of the additive concentrate of Example G. Example VIII An automatic transmission fluid as in Example VII wherein the oil is Exxon Dexron® II Base and 13.7% of the additive concentrate of Example H replaces that of Example G. The Fuel Compositions The Normally Liquid Fuels As indicated hereinabove, the products of this invention may also be used as additives for normally liquid fuels. The fuels used in the fuel compositions of this invention are well known to those skilled in the art and usually contain a major portion of a normally liquid fuel such as hydrocarbonaceous petroleum distillate fuel (e.g., motor gasoline as defined by ASTM Specifications D-439-89 and D-4814-91 and diesel fuel or fuel oil as defined in ASTM Specifications D-396-90 and D-975-91). Fuels containing non-hydrocarbonaceous materials such a alcohols, ether, organo-nitro compounds and the like (e.g., methanol, ethanol, diethyl ether, methyl ethyl ether, nitromethane) are also within the scope of this invention as are liquid fuels derived from vegetable or mineral sources. Vegetable or mineral sources include, for example, crude petroleum oil, coal, corn, shale, oilseeds and other sources. Oxygenates are compounds covering a range of alcohol and ether type base fuel. They have also been used as the sole fuel component, but more often as a supplemental fuel used together with, for example, gasoline to form the well-known "gasohol" blend fuels. Oxygenate-containing fuels are described in ASTM D-4814-91. Methanol and ethanol are commonly used oxygenates. They are primarily used as fuels. Other oxygenates, such as ethers, for example methyl-t-butyl ether, are more often used as octane number enhancers for gasoline. Mixtures of fuels are useful. Examples of fuel mixtures are combinations of gasoline and ethanol, diesel fuel and ether, gasoline and nitromethane, etc. Particularly preferred fuels are gasoline, that is, a mixture of hydrocarbons having an ASTM boiling point of 60°C at the 10% distillation point to about 205°C at the 90% distillation point, oxygenates, and gasoline-oxygenate blends, all as defined in the aforementioned ASTM Specifications for automotive gasolines. Most preferred is gasoline. The fuel compositions of the present invention may contain other additives which are well known to those of skill in the art. These can include anti-knock agents such as tetra-alkyl lead compounds, lead scavengers such as halo-alkanes, dyes, antioxidants such as hindered phenols, rust inhibitors such as alkylated succinic acids and anhydrides and derivatives thereof, bacteriostatic agents, auxiliary dispersants and detergents, gum inhibitors, fluidizers, metal deactivators, demulsifiers, anti-icing agents and the like. The fuel compositions of this invention may be lead-containing or lead-free fuels. Preferred are lead-free fuels. The products of this invention provide a number of benefits to a treated fuel, including detergency, anticorrosion and the like. In one particular embodiment of this invention, the motor fuel compositions contain an amount of additives sufficient to provide total intake system cleanliness. In another embodiment, they are used in amounts sufficient to prevent or reduce the formation of intake valve deposits or to remove them where they have formed. As mentioned hereinabove, fluidizers may be used in the fuel compositions of the instant invention. Useful fluidizers include natural oils or synthetic oils, or mixtures thereof. Natural oils include mineral oils, vegetable oils, animal oils, and oils derived from coal or shale. Synthetic oils include hydrocarbon oils such as alkylated aromatic oils, olefin oligomers, esters, including esters of polycarboxylic acids, polyols, polyethers, poly(oxyalkylene) glycols, alkylphenol-derived polyethers, and others. Fluidizers are usually fuel soluble, meaning they are soluble in the fuel in amounts of at least 0.1% by weight, more preferably at least 1% by weight. Certain fluidizers, for example, butylene- and propylene oxide derived fluidizers, are generally soluble in fuels at all levels. These are readily prepared from alcohol, glycol and phenol initiators under superatmospheric conditions, preferably in the presence of basic catalysts. Especially preferred mineral oils are paraffinic oils containing no more than 20% unsaturation, that is, no more than 20% of the carbon to carbon bonds are olefinic. Particularly useful synthetic oils are the polyether oils such as those marketed under the UCON® tradename by Union Carbide Corporation, poly(oxyalkylene) glycols such as those marketed under the EMKAROX® tradename by ICI Chemicals and described in EP 0647700-A1 based on USSN 133442 filed October 6, 1993.and polyester oils derived from a polyol and one or more monocarboxylic acids such as those marketed by Hatco Corporation. Other examples are polyoxyalkylene compounds prepared from C 1-30 alcohols or C 7-24 alkylphenols and sufficient propylene- or butylene oxide such that molecular weight ranges from 200 to 5,000, and monoethers and N-vinylpyrrolidinone addition products thereof. Additional fluidizers include polyoxyalkylene compounds prepared from glycols or polyols having from 2 to 10 carbon atoms and sufficient propylene- or butylene oxide such that overall molecular weight ranges from 200 to 6,000 and ether derivatives thereof. Preferably, the fluidizers have a kinematic viscosity ranging from 2 x 10 -6 to 2.5 x 10 -5 m 2 .s -1 (2 to 25 centistokes) at 100°C, preferably from 4 x 10 -6 to 2.0 x 10 -5 m 2 .s -1 (4 to 20 centistokes), and often up to 1.5 x 10 -5 m 2 .s -1 (15 centistokes). If the viscosity of the fluidizer is too high, a problem that may arise is the development of octane requirement increase (ORI) wherein the octane value demands of the engine tend to increase with time of operation. While both mineral oils and synthetic oils are generally useful as fluidizers over the entire preferred viscosity range, it has been observed that at the lower end of the viscosity range, synthetic oils tend to provide somewhat superior performance compared to mineral oils. It has been found that fluidizers, particularly when used within the ranges specified herein, together with the compositions of this invention, improve detergency and emissions, and reduce the tendency toward valve sticking. Amounts of the various additives, including individual amounts to be used in the fuel composition, and relative amounts of additives are given hereinafter. The fuel compositions of this invention may contain auxiliary dispersants. A wide variety of dispersants are known in the art and may be used together with the amide compounds described herein. Preferred auxiliary dispersants are Mannich type dispersants, acylated nitrogen-containing dispersants, aminophenol dispersants, aminocarbamate dispersants, ester dispersants and amine dispersants. Acylated nitrogen-containing compounds include reaction products of hydrocarbyl-substituted carboxylic acylating agents such as substituted carboxylic acids or derivatives thereof with ammonia or amines. Especially preferred are succinimide dispersants. Acylated nitrogen-containing compounds are known in the art and are disclosed in, for example, US Patents 4,234,435; 3,215,707; 3,219,666; 3,231,587 and 3,172,892. The auxiliary dispersant may also be an ester. These compounds are prepared by reacting a hydrocarbyl-substituted carboxylic acylating agent with at least one organic hydroxy compound. In another embodiment, the ester dispersant is prepared by reacting the acylating agent with a hydroxyamine. Preferred are succinic esters. Carboxylic esters and methods of making the same are known in the art and are disclosed in U.S. Patent 3,219,666, 3,381,022, 3,522,179 and 4,234,435. The carboxylic esters may be further reacted with at least one amine and preferably at least one polyamine. These nitrogen-containing carboxylic ester dispersant compositions are known in the art, and the preparation of a number of these derivatives is described in, for example, U.S. Patents 3,957,854 and 4,234,435. Also included among the auxiliary dispersants are Mannich type dispersants. Mannich products are formed by the reaction of at least one aldehyde, at least one amine having at least one N-H group and at least one hydroxyaromatic compound. Mannich products are described in the following patents: U.S. Patent 3,980,569; U.S. Patent 3,877,899; and U.S. Patent 4,454,059. The auxiliary dispersant may be a polyalkene-substituted amine. Polyalkene-substituted amines are well known to those skilled in the art. Typically, polyalkene-substituted amines are prepared by reacting olefins and olefin polymers (polyalkenes) and halogenated derivatives thereof with amines (mono- or polyamines). These amines are disclosed in U.S. patents 3,275,554; 3,438,757; 3,454,555; 3,565,804; 3,755,433; and 3,822,289. Aminophenols are also included among useful auxiliary dispersants that may be used in the fuel composition of this invention. Typically, such materials are prepared by reducing hydrocarbyl substituted nitrophenols to the corresponding aminophenol. Useful aminophenols include those described in Lange, US Patents 4,320,000 and 4,320,021. Aminophenols and methods for preparing are described in US patents 4,100,082 and 4,200,545 to Clason et al, US Patent 4,379,065 (Lange) and US 4,425,138 (Davis). It should be noted that the term "phenol" used in the context of aminophenols is not intended to limit the compounds referred to in that manner as being only hydroxybenzene derivatives. The term "phenol" is intended to encompass hydroxy aromatic compounds, including hydroxybenzene compounds, naphthols, catechols and others as described in the foregoing patents. Also included among useful auxiliary dispersants are aminocarbamate dispersants such as those described in US Patent 4,288,612. Treating levels of the additives used in this invention are often described in terms of pounds of additive per thousand barrels (PTB) of fuel. PTB values may be converted to approximate values expressed as parts (by weight) per million parts (by weight) of fuel by multiplying PTB by 4 for gasoline and by 3.3 for diesel oil and fuel oil. To determine precise values it is necessary that the specific gravity of the fuel is known. The skilled person can readily perform the necessary mathematical calculations. The fuel compositions of this invention may contain from 0.014 to 1.4 kg. m -3 (5 to 500 pounds per thousand barrels (PTB)) of fuel additive, preferably from 0.029 to 0.7 kg.m -3 (10 to 250 PTB), more preferably from 0.057 to 0.29 kg.m -3 (20 to 100 PTB). Fluidizers, when used, are generally present in amounts ranging from 0.0029 to 1.4 kg.m -3 (1 to 500 PTB), more often from 0.029 to 0.7 kg.m -3 (10 to 250 PTB) and most preferably from 0.029 to 0.43 kg.m -3 (10 to 150 PTB). Relative amounts by weight, of the nitrogen-containing compound to fluidizer oil typically range from 1:0 that is, essentially free of fluidizer, up to 1:10, more often from 1:0.5 - 2:0, preferably from 1:0.75 - 1.25. Additive Concentrates As mentioned hereinabove, the additives for use in fuels may be supplied as additive concentrates which are then diluted with normally liquid fuels. The following Table illustrates additive concentrates for use in fuels. Concentrate (% by Weight) Component F-I F-II F-III F-IV Alkylated aromatic hydrocarbon 15.76 19.2 15.76 19.2 Product of Example 2B 33.38 38 Product of Example 3 33.38 38 Demulsifiers 0.22 0.22 Polyether Oil 42.8 42.8 Propoxylated succinic acid Mineral oil 45.94 45.94 21.37 2-Ethylhexanol 4.54 4.54 The following examples illustrate several fuel compositions of this invention. When referring to compounds described in Examples 1-32, amounts are given in parts and percentages by weight as prepared. Unless indicated otherwise, all other parts and percentages are by weight and amounts of additives are expressed in amounts substantially free of mineral oil or hydrocarbon solvent diluent. The abbreviation 'PTB' means pounds of additive per thousand barrels of fuel. The following Tables illustrate several fuel compositions of the instant invention comprising unleaded gasoline and the indicated amounts of additive in percent by weight concentrate in fuel. UNLEADED GASOLINE + % WEIGHT ADDITIVE CONCENTRATE Example Concentrate F-A F-B F-C F-D F-E F-I 0.08 F-II 0.07 F-III 0.08 F-IV 0.0007 0.015 UNLEADED GASOLINE + 0.14 kg.m -3 (50 PTB) PRODUCT Example F-F F-G F-H F-I F-J 2-B 3 37 27 28 While the invention has been explained in relation to its preferred embodiments, it is to be understood that various modifications thereof will become apparent to those skilled in the art upon reading the specification. Therefore, it is to be understood that the invention disclosed herein is intended to cover such modifications that fall within the scope of the appended claims.

Claims: A process comprising first reacting, optionally in the presence of an acidic catalyst selected from organic sulfonic acids, heteropolyacids, Lewis acids, and mineral acids, (A) at least one olefinic compound containing at least one group of the formula and (B) at least one carboxylic reactant selected from compounds of the formula R 3 C(O)(R 4 ) n C(O)OR 5 (IV) and compounds of the formula wherein each of R 3 , R 5 and R 9 is independently H or a hydrocarbyl group, R 4 is a divalent hydrocarbylene group, and n is 0 or 1; wherein (A) and (B) are reacted in an amount of from more than 1.5 moles (B) per mole of (A) up to 3 moles (B) per equivalent of (A); then reacting the product formed thereby with from 0.5 equivalents up to 2 moles, per mole of (B) of at least one of (C) ammonia or a hydrazine or an amine characterized by the presence within its structure of at least one H-N group. The process of claim 1 wherein the at least one reactant (B) is selected from glyoxylic acid and a compound of the formula wherein R 3 is H and R 5 and R 9 are independently lower alkyl groups selected from methyl, ethyl, propyl and butyl, and n = 0; and (A) the olefinic compound has M n of from 100 to 70,000 and the general formula (R 1 )(R 2 ) C=C(R 6 )(CH(R 7 )(R 8 )) (III) wherein each of R 1 and R 2 is, independently, hydrogen or a hydrocarbon based group and each of R 6 , R 7 and R 8 is, independently, hydrogen or a hydrocarbon based group. The process of claim 2 wherein each of R 1 and R 2 is hydrogen and R 6 is H or a lower alkyl group and the group (CH(R 7 )(R 8 )) is a hydrocarbyl group containing from 7 to 5000 carbon atoms. The process of claim 3 wherein the group (CH(R 7 )(R 8 )) is an aliphatic group containing from 30 to 200 carbon atoms and the olefinic compound is derived from homopolymerized and interpolymerized C 2-8 olefins. The process of claim 4 wherein the olefinic compound is a polyolefin comprising a mixture of isomers, at least 50% by weight of the mixture comprising isomers of the formula H 2 C = C(R 6 )(CH(R 7 )(R 8 )) wherein R 6 is H or lower alkyl. The process of claim 5 wherein the polyolefin is a polybutene and R 6 is methyl. The process of claim 2 wherein the olefinic compound is a polyolefin comprising a mixture of isomers wherein from 50% to 65% are trisubstituted olefins wherein one substituent contains from 2 to 5000 carbon atoms and the other two substituents are lower alkyl. The process of claim 2 wherein the olefinic compound is a linear α-olefin containing from 8 to 28 carbon atoms. The process of claim 1 wherein the olefinic compound is an ethylene-alpha-olefin copolymer. The process of claim 1 wherein the olefinic compound is an ethylene-alpha olefin-diene terpolymer. The process of claim 1 wherein the olefinic compound is a polyolefinic compound. The process of any preceding claim wherein (C) is at least one of an alkylene polyamine, an alkylene bottoms product, and a condensed polyamine derived from at least one hydroxy-containing material and at least one alkylene polyamine or alkylene polyamine bottoms product. An additive concentrate for formulating lubricating oil or fuel compositions comprising from 20% to 99% by weight of a normally liquid, substantially inert organic diluent and from 10% to 80% by weight of a composition prepared by the process of any one of claims 1-12. A lubricating composition comprising a major amount of an oil of lubricating viscosity and a minor amount of a composition prepared by the process of any one of claims 1-12. A fuel composition comprising a major amount of a normally liquid fuel and a minor amount of a composition prepared by the process of any one of claims 1-12 and optionally further comprising a fluidizer.

Inventors: ADAMS PAUL E, BAKER MARK R, DIETZ JEFFRY G, ADAMS, PAUL E., BAKER, MARK R., DIETZ, JEFFRY G.
Applicants: LUBRIZOL CORP, THE LUBRIZOL CORPORATION
Application year: 1997
Main classification: C10M133
IPC codes: C10L1, C10M133, C10M159, C08F8, C10L10