N-substituted carbamates and their use as gasoline additives

Abstract: The invention provides polyolefin-polyamine-N-substituted polycarbamates, useful for preventing or reducing deposits in engines, of the general formula: wherein n is 2 to 8; R¹ represents a polyolefin chain having a number average molecular weight (M n ) in the range from 500 to 9900; each R² independently represents a C₂-C₈ alkylene group; R³ represents a hydrogen atom or a C₁-C₇ alkyl group; each R⁴ independently represents a hydrogen atom, a C₁-C₇ alkyl group, or -COOR⁵ with at least two of R⁴ being -COOR⁵ and wherein each R⁵ independently represents a hydrocarbyl or substituted hydrocarbyl group containing up to 20 carbon atoms; a process for their preparation; and gasoline compositions and gasoline additive concentrates containing them.

Description: The present invention relates to certain polyolefin-polyamine-N-substituted carbamates, a process for their preparation, and gasoline compositions and gasoline additive concentrates containing them. It is known that during the initial operation of a new or clean internal combustion engine, a gradual increase in octane requirement (OR), i.e., the fuel octane number required for knock-free operation, increases with the build-up of combustion chamber deposits until a stable level is reached which generally corresponds to a time when deposits remain relatively constant. The actual stable level can vary with engine design and even with individual engines of the same design. Many additives are known which can be added to hydrocarbon fuels to attempt to prevent or reduce deposit formation or remove or modify formed deposits in the combustion chamber and adjacent surfaces, such as valves, ports, and spark plugs, in order to reduce octane requirement. Continued improvement in design of internal combustion engines, e.g., fuel injection engines, brings changes to the atmosphere of the combustion chamber so there is a continuing need for new additives to control the problem of deposits and improve driveability which is usually related to deposits. WO-A-8810250 discloses, in the first aspect, a process for the production of a carbamate having the formula: wherein X and Y are independently either hydrogen, a hydrocarbyl group or a hetero-substituted hydrocarbyl group or the group of formula: wherein Z is either a divalent hydrocarbyl or substituted hydrocarbyl group or a group of the formula: [ (alkylene) m (NH) n (alkylene) m ] in which n = 0 to 4 and m = 1 to 4, and R is a hydrocarbyl or substituted hydrocarbyl group, provided that if either one of X or Y is the group of formula (B), the other of X or Y is hydrogen, which process comprises reacting either a compound of the formula: wherein X and Y are independently either hydrogen, a hydrocarbyl group, or a hetero-substituted hydrocarbyl group, with a dihydrocarbyl carbonate having the formula: wherein independently R is as defined above in the presence as catalyst of a strong organic base and in the proportions necessary to produce either a mono-carbamate or a bis-carbamate. WO-A-8810250 also discloses an internal combustion engine fuel concentrate composition comprising as a first component from 1 to 95% by weight of a carbamate of the formula (A) wherein the group R is a hydrocarbyl or substituted hydrocarbyl group of a molecular weight and composition such as to impart fuel solubility as produced by the above process and as a second component a fuel compatible solvent therefor; and further discloses an internal combustion engine fuel composition comprising a major proportion of an internal combustion engine fuel, preferably a fuel boiling in the gasoline range, and a minor proportion of the concentrate composition as hereinbefore described. Additive molecules that liberate carbon dioxide under thermal conditions have been found to aid in the control and/or removal of deposits. U.S. Patent No. 4,936,868 discloses the use of certain polyolefin-N-substituted carbamates as a deposit preventing or reducing additive in gasolines. These additive molecules have one carbon dioxide producing carbamate group per molecule. To increase the carbon dioxide producing effect of this additive in a gasoline requires increasing the amount of additive present, which can result in undesired side effects. In accordance with the present invention, there is provided polyolefin-polyamine-N-substituted polycarbamates, useful for preventing or reducing deposits in engines of the general formula: wherein n is 2 to 8, preferably 3 to 5; R 1 represents a polyolefin chain having a number average molecular weight (M n ) in the range from 500 to 9900, preferably from 550 to 4900 and most preferably from 600 to 1300; each R 2 independently represents a C 2 -C 8 , preferably C 2 -C 5 , alkylene group; R 3 represents a hydrogen atom or a C 1 -C 7 alkyl, preferably a methyl or ethyl, group; each R 4 independently represents a hydrogen atom, a C 1 -C 7 alkyl, preferably a methyl or ethyl, group, or -COOR 5 with at least two of R 4 being -COOR 5 and wherein each R 5 independently represents a C 1 -C 4 alkyl group. Preferably, in formula I, n is 3 to 5; R 1 represents a polyisobutylene chain having a number average molecular weight from 600 to 1300; each R 2 independently represents a C 2 -C 5 alkylene group; R 3 is a hydrogen atom or a methyl or ethyl group; each R 4 independently represents a hydrogen atom, a methyl or ethyl group, or -COOR 5 with at least three of R 4 being -COOR 5 and wherein each R 5 independently represents a C 1 -C 4 alkyl group. The polyolefin-polyamine-N-substituted carbamates of formula I above are a new class of additives, useful in gasoline for preventing deposits in engines while also readily breaking down cleanly producing very little residue and are miscible with carriers, such as polymeric olefins. Spark plugs from some engines run on some of the gasolines containing the polyolefin-polyamine-N-substituted carbamates of formula I were found to be exceptionally clean. Examples of compounds of formula I are those in which: R 1 R 2 R 3 R 4 n polyisobutylene ethylene hydrogen bis-hydrogen + bis-methylcarboxyl 3 polyisobutylene propylene methyl bis-methyl + tris-methylcarboxyl 4 R 1 R 2 R 3 R 4 n polyisobutylene isobutylene methyl methyl + tetra-isobutylcarboxyl 4 polyisobutylene isobutylene methyl methyl + bis-isobutylcarboxyl + bis-methylcarboxyl 4 The compounds of formula I may conveniently be prepared by treating a polyolefin-secondary-polyamine intermediate as described hereinafter with a compound of the general formula: in which Z represents a halogen atom, or an alkoxy, e.g. C 1-6 alkoxy, or alkylthio, e.g. C 1-6 alkythio, group and R 5 is as defined above. The compounds of formula II are generally available in the art. Suitable such halides or esters of formula II include carbonates and thiocarbonates. R 5 is an alkyl group containing 1 to 4 carbon atoms, such as a methyl, ethyl, n-propyl, isopropyl, n-butyl or isobutyl group. Preferably, R 5 is a methyl, ethyl, propyl, n-butyl or isobutyl group. Z is preferably a halogen, such as chlorine. At least two moles, more preferably at least three moles and most preferably at least four moles of a compound of formula II are used for each mole of polyolefin-secondary-polyamine intermediate. Two or more different compounds of formula II having different R 5 groups may be used in the reaction mixture to produce a product having different alkyl carbamate moieties on the nitrogen atoms. Alternatively, one compound of formula II may be reacted with the polyamine intermediate under conditions to provide incomplete substitution of the nitrogen atoms with carbamate moieties, the product subsequently recovered and then the reaction cycle repeated with the product and a different compound of formula II to provide a further product having different alkyl carbamate moieties on the nitrogen atoms. The reaction to produce the compounds of formula I is usually conducted in a solvent which is non-reactive with chloroformates and which solubilizes the two reactants, e.g. hydrocarbon solvents such as toluene and xylene. The reaction is conveniently conducted under relatively moderate conditions, e.g. at ambient pressure and at a temperature in the range from 0 to 40°C. Other moderate temperatures and pressures can be used which will not decompose the desired product. The compound of formula I is recovered by conventional techniques, such as drying by stripping water or by using anhydrous sodium sulphate. The solvent is usually removed, e.g., by stripping, for neat analysis. However, for practical applications some or all of the solvent can be retained as a diluent. Small amounts of unreacted polyolefin-secondary-polyamine intermediate need not be removed from the product as the presence thereof does not interfere with the usefulness of the product of formula I. Unreacted amine can aid in the effects of the polyolefin-polyamine-N-substituted polycarbamates of the invention by acting as a carrier, assisting in enhancing the preventing, removing or retarding of engine deposits (particularly when the carbamate is of methyl or a non-beta hydrogen group), or by providing their known fuel detergent properties. Other known materials for use in fuels can also serve one or more of these purposes, including the polymer additives described hereinafter. The polyolefin-secondary-polyamine intermediates can be prepared by reacting olefinic polymers with polyamines employing conventional procedures as hereinafter described. These oil soluble polyolefin-secondary polyamine intermediates contain a polymer chain having a number average molecular weight (M n ) in the range from 500 to 9,900, preferably from 550 to 4,900, and particularly from 600 to 1,300, which can be saturated or unsaturated and straight or branched chain and which is attached to a nitrogen atom of the polyamine-derived moiety. The polyolefin-secondary-polyamine intermediates are compounds of the general formula: wherein n, R 1 , R 2 and R 3 are as defined above, and each R 3' independently represents a hydrogen atom or a C 1 -C 7 alkyl group provided that at least two of R 3' are hydrogen atoms. The present invention further provides a process for the preparation of a compound of formula I as defined above which comprises reacting at least one compound of formula II as defined above with a compound of formula III as defined above, the molar ratio of total compound or compounds of formula II to compound of formula III being at least 2:1, preferably in the range 2:1 to 10:1. Where more than one compound of formula II is reacted, the compounds of formula II may be reacted simultaneously or sequentially. The olefinic polymers (R 1 in formulae I and III) which are reacted with polyamines to form the polyolefin-secondary-polyamine intermediates used in the present invention are known in the art, e.g. from U.S. Patent No. 4,357,148, and include olefinic polymers derived from alkanes or alkenes with straight or branched chains, which may or may not have aromatic or cycloaliphatic substituents, for instance, groups derived from polymers or copolymers of olefins which may or may not have a double bond. Examples of non-substituted alkenyl and alkyl groups are polyethylene groups, polypropylene groups, polybutylene groups, polyisobutylene groups, polyethylene-polypropylene groups, polyethylene-polyalpha-methyl styrene groups and the corresponding groups without double bonds. Particularly preferred are polypropylene and polyisobutylene groups. The polyamines used to react with the olefinic polymers to form the polyolefin-secondary-polyamine intermediates of formula III above are preferably ethylene diamine, diethylene triamine, triethylene tetramine, tetraethylene pentamine, tripropylene tetramine, pentapropylene hexamine, triisobutylene tetramine, tetraisobutylene pentamine, triisoamylene tetramine, tetraisoamylene pentamine, pentaisoamylene hexamine and higher homologues up to 35 carbon atoms. Compounds possessing triamine as well as tetramine and pentamine groups are preferred for use because these can be prepared from technical mixtures of polyethylene polyamines, which offer economic advantages. An example of a suitable process for the preparation of the polyolefin-secondary-polyamine intermediates employed according to the invention is the reaction of a halogenated hydrocarbon having a halogen atom as a substituent and a hydrocarbon chain as defined hereinbefore with a polyamine. The halogen atom is replaced by a polyamine group, while hydrogen halide is formed. The hydrogen halide can then be removed in any suitable way, for instance, as a salt with excess polyamine. The reaction between halogenated hydrocarbon and polyamine is preferably effected at elevated temperature in the presence of a solvent; particularly a solvent having a boiling point of at least 160°C. The present invention further provides a gasoline composition comprising a major amount of a gasoline and from 20 to 1000 ppmw, based on the total weight of the gasoline composition, of a compound of formula I as defined above. Suitable liquid hydrocarbon fuels in the gasoline boiling range are mixtures of hydrocarbons having a boiling point in the range from 25°C to 232°C, and comprise mixtures of saturated hydrocarbons, olefinic hydrocarbons and aromatic hydrocarbons. Preferred are gasoline blends having a saturated hydrocarbon content ranging from 40 to 80 per cent volume, an olefinic hydrocarbon content ranging from 0 to 30 per cent volume and an aromatic hydrocarbon content ranging from 10 to 60 per cent volume. The base fuel can be derived from straight run gasoline, polymer gasoline, natural gasoline, dimer and trimerized olefins, synthetically produced aromatic hydrocarbon mixtures, from thermally or catalytically reformed hydrocarbons, or from catalytically cracked or thermally cracked petroleum stocks, and mixtures of these. The hydrocarbon composition and octane level of the base fuel are not critical. The octane level, (R+M)/2, will generally be above 85. Any conventional motor fuel base can be employed in the practice of this invention. For example, in the gasoline, hydrocarbons can be replaced by up to substantial amounts of conventional alcohols, or ethers, conventionally known for use in fuels. The base fuels are desirably free of water, since water could impede a smooth combustion. Preferably, the gasolines used in the present invention are lead-free, but may contain minor amounts of blending agents such as methanol, ethanol and ethyl tertiary butyl ether at from 0.1 to 15% volume of the base fuel. The fuels can also contain antioxidants such as phenolics, e.g., 2,6-di-tert-butylphenol or phenylenediamines, e.g., N,N'-di-sec-butyl-p-phenylenediamine, dyes, metal deactivators and dehazers such as polyester-type ethoxylated alkylphenol-formaldehyde resins. Corrosion inhibitors, such as a polyhydric alcohol ester of a succinic acid derivative having on at least one of its alpha-carbon atoms an unsubstituted or substituted aliphatic hydrocarbon group having from 20 to 500 carbon atoms, for example, pentaerythritol diester of polyisobutylene-substituted succinic acid, the polyisobutylene group having a number average molecular weight of 950, in an amount of 1 to 1000 ppmw. The fuels can also contain antiknock compounds such as methyl cyclopentadienylmanganese tricarbonyl, ortho-azidophenol as well as co-antiknock compounds such as benzoyl acetone. An effective amount of polyolefin-polyamine-N-substituted polycarbamate(s) of the present invention can be introduced into the combustion zone of the engine in a variety of ways to prevent build-up of deposits, or to accomplish reduction or modification of deposits. Thus, the polyolefin-polyamine-N-substituted polycarbamate(s) can be injected into the intake manifold intermittently or substantially continuously, as described, preferably in a hydrocarbon carrier having a final boiling point (by ASTM D86) lower than 232°C. A preferred method is to add the agent to the gasoline. For example, the agent can be added separately to the gasoline or blended with other additives. The effective amount of polyolefin-polyamine-N-substituted polycarbamate(s) of the invention used will of course depend on the particular compound(s) used, the engine and the gasoline and carrier types. Thus, the total amount of polyolefin-polyamine-N-substituted polycarbamate(s) used will range from 20 to 1000, preferably from 50 to 750, and most preferably from 100 to 500 ppm by weight based on the total weight of the gasoline composition. For use in the gasoline compositions of the invention, mixtures of different polyolefin-polyamine-N-substituted polycarbamates can be used. For example, a mixture where R 5 of formula I is methyl and is isobutyl. The polyolefin-polyamine-N-substituted polycarbamates of the invention can also be used in combination with certain polymeric components which are polymers of monoolefins having up to 6 carbon atoms; poly(oxyalkylene) alcohols, glycols or polyols; or polyolefin amines. Such materials are well known in the art. For example, polymers of monoolefins are described in U.S. Patents Nos. 2,692,257, 2,692,258, 2,692,259, 2,918,508, and 2,970,179. Such polymers include (1) polymers of C 2 to C 6 monoolefins, (2) copolymers of C 2 to C 6 monoolefins, (3) the corresponding hydrogenated polymer (1) or copolymer (2), or (4) mixtures of at least two of (1), (2) and (3), the polymeric component having a number average molecular weight as determined by osmometry in the range from 500 to 3500, preferably from 500 to 1500. Particularly preferred are those having a number average molecular weight in the range from 600 to 950. Mixtures of polymers wherein a substantial portion of the mixture has a molecular weight above 1500 are considerably less effective. The polyolefins may be prepared from unsaturated hydrocarbons having from 2 to 6 carbon atoms, e.g. ethylene, propylene, butylene, isobutylene, butadiene, amylene, isoprene, and hexene. Preferred for their efficiency and commercial availability are (hydrogenated) polymers of propylene and butylene; particularly preferred are (hydrogenated) polymers of polyisobutylene. Poly(-C 2 to C 6 -oxyalkylene) alcohols, glycols and polyol carriers can be used singly or in mixtures, such as the "Pluronics" (Trade mark) fluids marketed by BASF Wyandotte Corp., and the "UCON LB" (Trade Mark) series fluids marketed by Union Carbide Corp. Preferably, these carriers include poly(oxypropylene) alcohol, glycol or polyol of number average molecular weight of 300 to 4000, which may or may not be capped by an alkyl group, e.g., a (C 1-10 hydrocarbyl)poly(oxypropylene) alcohol and polyethylene glycols of number average molecular weight from 300 to 4000. The polyolefin amines of a C 2 to C 6 monoolefin, described hereinbefore for use as the starting materials used to make the compounds of formula I are also useful as the polyolefin amine fuel additives. The present invention further provides a gasoline additive concentrate comprising (a) from 25 to 500 ppm by weight (preferred from 50 to 200 ppm) of a compound of formula I as defined above; (b) from 10 to 1000 ppm (preferably 50-400 ppm) by weight of a polymeric component which is (i) a polymer of a C 2 to C 6 monoolefin, (ii) a copolymer of a C 2 to C 6 monoolefin, (iii) the corresponding hydrogenated polymer or copolymer, (iv) a poly(oxy-C 2 to C 6 -alkylene) alcohol, glycol or polyol, (v) a polyolefin amine of a C 2 to C 6 monoolefin, or (vi) a mixture of at least two of (i), (ii), (iii) (iv) and (v); (c) optionally up to 20 ppm by weight of a dehazer; and (d) balance a gasoline compatible diluent, e.g. a gasoline compatible diluent boiling in the range from 50°C to 232°C, all amounts being based on the total weight of the gasoline additive concentrate. Very suitable diluents include oxygen-containing hydrocarbons and non-oxygen-containing hydrocarbons. Suitable oxygen-containing hydrocarbon diluents include, e.g., methanol, ethanol, propanol, methyl tert-butyl ether and ethylene glycol monobutyl ether. The diluent can be an alkane such as heptane, but preferably is an aromatic hydrocarbon such as toluene, xylene alone or in admixture with said oxygen-containing hydrocarbon diluents. Optionally, the concentrate can contain up to 20 ppm by weight of a dehazer, particularly a polyester-type ethoxylated alkylphenol-formaldehyde resin, or other conventional dehazer. The present invention still further provides the use of from 20 to 1000 ppmw, based on total composition, of a compound of formula I as defined above, as a deposit preventing or reducing additive in a gasoline composition comprising a major amount of a gasoline. The invention will be further understood from the following illustrative examples. Example 1 Preparation of a Compound of Formula I with the following: a) n being 4; b) R 3 being hydrogen; c) one R 4 being hydrogen; d) four R 4 s being -COOR 5 ; e) all of the R 5 s being isobutyl; f) R 1 being polyisobutylene of number average molecular weight 950; and g) each R 2 being ethylene. The above compound is hereinafter referred to as Isobutyl(4)PIB-TEPA-CARB, PIB referring to polyisobutylene, TEPA referring to tetraethylene pentamine and CARB referring to carbamate. 300 Grams (0.26 mol) of polyisobutylene-(NHCH 2 CH 2 ) 4 -NH 2 (PIB-TEPA) and 76 grams (0.83 mol) of toluene were charged to a 1000 ml, round-bottomed flask equipped with an air-driven stirrer, reflux condenser, thermometer, and addition funnel. To the addition funnel were added 153 grams (1.12 mol) of i-butyl chloroformate and 59 grams (0.64 mol) of toluene (molar ratio i-butyl chloroformate: PIB-TEPA being 4.3:1). The toluene solution was added dropwise at ambient temperature (20°C) to the round-bottomed flask with stirring. The addition took about 50 minutes with an increase of 40°C in reaction temperature. The reaction flask was heated to reflux after the addition was completed and maintained at that temperature for 4 hours. The reaction temperature was dropped to 40°C. The addition funnel was removed and replaced with a powder funnel. Through this latter funnel was added a solution of 121 grams (1.14 mol) of sodium carbonate in 484 grams (26.89 mol) of water. Upon completion of the addition, the flask was heated to reflux for 6 hours. The contents of the reaction flask were transferred to a 2000 ml separatory funnel where the layers were separated and the lower water layer was removed. The remaining layer was treated with 250 ml of water until the water layer gave a neutral pH. The water was removed and the contents of the funnel were transferred to a 2000 ml Erlenmeyer flask. 250 Milliliters of toluene and about 5 grams (0.04 mol) of anhydrous sodium sulphate were added to the flask. After 4 hours of stirring, the contents of the Erlenmeyer flask were filtered and solvent removed by rotary evaporation. Evaluation of the neat material revealed a basic nitrogen content of 0.73%w and a total nitrogen of 2.97%w confirming that 3.8 or approximately four of the five nitrogens had reacted and were now rendered non-basic. Examination by Infrared Spectroscopy (IR) showed a typical carbamate absorption at 1700 cm -1 (uncorrected). Example 2 Preparation of a Compound of Formula I with the following: a) n being 4; b)* R 3 and one R 4 being methyl or hydrogen; c) four R 4 s being -COOR 5 ; d) two of the R 5 s being isobutyl and two of the R 5 s being methyl; e) R 1 being polyisobutylene of number average molecular weight 950; and f) each R 2 being ethylene. The above compound is hereinafter referred to as Isobutyl(2)methyl(2)PIB-TEPA-CARB. This compound was prepared in the same manner as in Example 1 except that 74 grams (0.54 mol) of i-butyl chloroformate and 58 grams (0.61 mol) of methyl chloroformate were reacted with the PIB-TEPA (molar ratio i-butyl and methyl chloroformates: PIB-TEPA being 4.4:1). Evaluation of the product revealed a basic nitrogen content of 0.7%w and a total nitrogen of 2.3%w confirming that 3.8 or approximately four of the five nitrogens had reacted and were now rendered non-basic. Examination by IR showed a typical carbamate absorption at 1700 cm -1 (uncorrected). Example 3 Preparation of a Compound of Formula I with the following: a) n being 4; b)* R 3 and two R 4 s being methyl or hydrogen; c) three R 4 s being -COOR 5 ; d) all of the R 5 s being methyl; e) R 1 being polyisobutylene of number average molecular weight 950; and f) each R 2 being ethylene. The above compound is hereinafter referred to as Methyl(3)PIB-TEPA-CARB. This compound was prepared in the same manner as in Example 1 except that 103 grams (1.09 mol) of methyl chloroformate were reacted with the PIB-TEPA(molar ratio methyl chloroformate: PIB-TEPA being 4.2:1). Evaluation of the product revealed a basic nitrogen content of 1.01%w and a total nitrogen of 2.73%w confirming that 3.1 or approximately three of the five nitrogens had reacted and were now rendered non-basic. Example 4 Engine Tests Fuels with and without the additives of the instant invention were tested in a Ford 3.0 litre engine with Port Fuel Injection (PFI) for 100 hours to determine the effectiveness of the instant additives in reducing intake valve deposits. The base fuel comprised premium unleaded gasoline. The polyolefin-polyamine-N-substituted polycarbamates were those prepared in Examples 1, 2 and 3 above. The polycarbamates were used at a 200 ppm by weight level. Each engine was in clean condition at the start of the test, i.e., oil and filters were changed and all deposits had been removed from the intake manifolds, intake ports, intake valves and combustion areas of the engine. In order to test for the accumulation of deposits in the engine during each test, the engines were operated on a cycle consisting of idle mode and cruising modes of 30, 35, 45, 55 and 65 mph (48.3, 56.3, 72.4, 88.5 and 104.6 km/h respectively) with accelerations and decelerations. The tests were conducted for 100 hours and the weight of the intake valve deposits was measured. Results of these tests are set forth in Table 1 below. Comparison of Intake Valve Deposits for a Series of PIB-TEPA-polyCARBs Additive Average Deposit Weight, mg None 362 Isobutyl(4)PIB-TEPA-CARB (Ex. 1) 317 Isobutyl(2)methyl(2)PIB-TEPA-CARB (Ex. 2) 166 Methyl(3)PIB-TEPA-CARB (Ex. 3) 51 Results of these tests demonstrate that the polyolefin-polyamine-N-substituted polycarbamates of the invention are very useful in very significantly preventing the accumulation of deposits in the engines tested as compared to the effects of the base fuel as shown by the much lower average valve deposits.

Claims: A polyolefin-polyamine-N-substituted polycarbamate of the general formula: wherein n is 2 to 8; R 1 represents a polyolefin chain having a number average molecular weight (M n ) in the range from 500 to 9900; each R 2 independently represents a C 2 -C 8 alkylene group; R 3 represents a hydrogen atom or a C 1 -C 7 alkyl group; each R 4 independently represents a hydrogen atom, a C 1 -C 7 alkyl group, or -COOR 5 with at least two of R 4 being -COOR 5 and wherein each R 5 independently represents a C 1 -C 4 alkyl group. A polycarbamate according to claim 1, wherein R 1 represents a polyolefin chain having a number average molecular weight from 550 to 4900. A polycarbamate according to claim 2, wherein R 1 represents a polyolefin chain having a number average molecular weight from 600 to 1300. A polycarbamate according to any one of claims 1 to 3, wherein R 1 represents a polyisobutylene chain. A polycarbamate according to any one of the preceding claims, wherein n is 3 to 5; R 1 represents a polyisobutylene chain having a number average molecular weight from 600 to 1300; each R 2 independently represents a C 2 -C 5 alkylene group; R 3 is a hydrogen atom or a methyl or ethyl group; each R 4 independently represents a hydrogen atom, a methyl or ethyl group, or -COOR 5 with at least three of R 4 being -COOR 5 and wherein each R 5 independently represents a C 1 -C 4 alkyl group. A process for the preparation of a polyolefin-polyamine-N-substituted polycarbamate of formula I as claimed in any one of claims 1 to 5, which comprises reacting at least one compound of the general formula: with a compound of the general formula: wherein n, R 1 , R 2 , R 3 and R 5 are as defined in claim 1, Z represents a halogen atom or an alkoxy or alkylthio group, and each R 3' independently represents a hydrogen atom or a C 1 -C 7 alkyl group provided that at least two of R 3' are hydrogen atoms, the molar ratio of total compound or compounds of formula II to compound of formula III being at least 2:1. A gasoline composition comprising a major amount of a gasoline and from 20 to 1000 ppmw, based on the total weight of the gasoline composition, of a polyolefin-polyamine-N-substituted polycarbamate of formula I as claimed in any one of claims 1 to 5. A composition according to claim 7, wherein the amount of polyolefin-polyamine-N-substituted polycarbamate of formula I ranges from 100 to 500 ppm by weight based on the total weight of the gasoline composition. A gasoline additive concentrate comprising (a) from 25 to 500 ppm by weight of a polyolefin-polyamine-N-substituted polycarbamate of formula I as claimed in any one of claims 1 to 5; (b) from 10 to 1000 ppm by weight of a polymeric component which is (i) a polymer of a C 2 to C 6 monoolefin, (ii) a copolymer of a C 2 to C 6 monoolefin, (iii) the corresponding hydrogenated polymer or copolymer of (i) or (ii), (iv) a poly(oxy-C 2 to C 6 -alkylene) alcohol, glycol or polyol, (v) a polyolefin amine of a C 2 to C 6 monolefin, or (vi) a mixture of at least two of (i), (ii), (iii), (iv) and (v); (c) optionally up to 20 ppm by weight of a dehazer; and (d) balance a gasoline compatible diluent, all amounts being based on the total weight of the concentrate.

Inventors: JOHNSON THOMAS HOWARD, JOHNSON, THOMAS HOWARD
Applicants: SHELL INT RESEARCH, SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
Application year: 1992
Main classification: C10L1
IPC codes: C10L1, C07C269, C07C271