CA2469766A1 - Distillate fuel compositions for improved combustion and engine cleanliness - Google Patents

Distillate fuel compositions for improved combustion and engine cleanliness Download PDF

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Publication number
CA2469766A1
CA2469766A1 CA002469766A CA2469766A CA2469766A1 CA 2469766 A1 CA2469766 A1 CA 2469766A1 CA 002469766 A CA002469766 A CA 002469766A CA 2469766 A CA2469766 A CA 2469766A CA 2469766 A1 CA2469766 A1 CA 2469766A1
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fuel
fuel additive
calcium sulfonate
overbased calcium
alkyl
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Timothy J. Henly
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Afton Chemical Corp
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Afton Chemical Corp
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/02Use of additives to fuels or fires for particular purposes for reducing smoke development
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/143Organic compounds mixtures of organic macromolecular compounds with organic non-macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/182Organic compounds containing oxygen containing hydroxy groups; Salts thereof
    • C10L1/1822Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
    • C10L1/1824Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms mono-hydroxy
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/188Carboxylic acids; metal salts thereof
    • C10L1/1881Carboxylic acids; metal salts thereof carboxylic group attached to an aliphatic carbon atom
    • C10L1/1883Carboxylic acids; metal salts thereof carboxylic group attached to an aliphatic carbon atom polycarboxylic acid
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/198Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
    • C10L1/1985Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid polyethers, e.g. di- polygylcols and derivatives; ethers - esters
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/238Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/2383Polyamines or polyimines, or derivatives thereof (poly)amines and imines; derivatives thereof (substituted by a macromolecular group containing 30C)
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2431Organic compounds containing sulfur, selenium and/or tellurium sulfur bond to oxygen, e.g. sulfones, sulfoxides
    • C10L1/2437Sulfonic acids; Derivatives thereof, e.g. sulfonamides, sulfosuccinic acid esters
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/30Organic compounds compounds not mentioned before (complexes)
    • C10L1/305Organic compounds compounds not mentioned before (complexes) organo-metallic compounds (containing a metal to carbon bond)

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Abstract

The invention provides a distillate fuel additive composition, and also a fuel composition containing a distillate fuel. an overbased calcium sulfonate detergent, a succinimide dispersant, and an organomancanese compound. Also provided is a method for improving the cleanliness of diesel fuel intake systems by the combustion in said systems of a distillate fuel containing the fuel additive composition.

Description

DISTILLATE FUEL COMPOSITIONS FOR IMPROVED COMBUSTION ~,,t~_~5~9 AND ENGINE CLEANLINESS
I I (;1_D
The present invention relates to a synergistic interaction bchvcen an overbased calcium sulfonate detergent and <tn ashless succinimide dispersant that allows (car the formulation of improved distillate fuel additive packages. (n addition to the metallic:
detergent and the ashless dispcrsant, the additive compositions cont<rin an organometallic complex of manganese.
Distillate fuels treated with the additive compositions exhibit improved combustion because of the detergent and the organomctallic manganese compound and good fuel system cleanliness because of the detergent/dispersant interaction.
I3~\C:KGROUND
to i\ great deal of prior art has been devoted to formulating distillate fuel additive compositions to provide environmental benefits when the fuel is combusted.
Such benefits include, liar example. reduced emissions of no;~ious pollutants such as oxides of nitrogen and particulate matter. reduced acidity of emitted particulates, and better fuel economy (which amounts to lower emissions of carbon dioxide per amount of fuel bcwncd). The effects of these t5 fuels on the cleanliness of fuel systems, e_g., on the buildup of carbon and lacquer on the fuel injectors found in diesel engines, has received less study.
A need exists for a distillate fuel additive composition that provides for the simultaneous achievement of improved combustion, fuel and combustion. system cleanliness, improved fuel economy, and reduction in pollutant generation.
SUMMARY OF THE EMBODIMENTS
An embodiment presented herein provides a fuel additive composition comprising an organometallic manganese compound, an alkyl-substituted succinimide ashless dispersant, and an overbased calcium sulfonate detergent of TBN above about 200. In another embodiment the T BN
of the overbased calcium sulfonate is about 300.
Anotf~er embodiment provides a fuel comprising a major amount of a middle distillate fuel and a minor amount of a fuel additive composition comprising an organornetallic manganese compound, an alkyl-substituted succinimide ashless dispc:rsant, and an ovcrbased calcium sulfonate detergent of TBN above about 200.
Accordingly, in one example herein is provided a method of for improving the cleanliness of a fuel intake systems by use in the fuel intake system of a fuel containing a fuel additive composition comprising an organornetallic manganese compound, an alkyl-substituted succinimide ashless dispersant, and an overbased calcium sulfonate detergent of TBN about 300.
It is to be understood that both the foregoing general description and the following detailed description are exemplary and explanatory only and are intended to provide further explanation of the present invention. as claimed.
DETAILED DESCRIPTION OF EMBODIMENTS
In one embodiment is provided herein distillate fue~I additive compositions for use in distillate firets that provide enhanced fuel combustion and, at the same time, superior cleanliness of fuel intake systems. Distillate firels are defined herein as petroleum-based hydrocarbon fuels boiling in the range of about 140-3b0°C [284-680°F] and encompass diesel and biodiesel fuels, jet fuels, marine fuels and home heating oils. Distillate fuels containing the additive compositions of the invention show enhanced combustion characteristics.
If certain components of the additive packages described herein are present in specific proportions, fuels containing the additive packages also show excellent fuel injector cleanliness ..,~.~~

rr~-~s9n as measured by the Cummins i_,10 diesel detergency test. ~I his injector cleanliness is exhibited as an injector rating of at most 10.0 in the Cummins L10 diesel detergency test.
Other embodiments herein provide an additive composition, a distillate fuel containing the additive composition, and a method of improving the cleanliness of fuel intake systems by use of the fuel containing the additive composition.
In an embodiment, tile additive composition contains at least an organometallic complex of manganese, an overbased calcium sulfonate detergent and an ashless succinimide dispcrsant such that when the additive composition is dissolved in a distillate fuel, the following relationship is satisfied:
-0.159x + 0.243y - 0.0143xy < -8.4 where x = concentration of succinimide (in potu~ds per thousand barrels) y = concentration of overbased calcium sulfonate (in PTB) t 5 with the following limitations:
x = 20-35, preferably 25-30, and y = 10-120, preferably 30-50.
The organometallic manganese compound does not affect injector cleanliness. In an embodiment, the organometallic manganese compound may be present in the fuel at:
concentrations of up to about 20 PTB.
It has been discovered that the combustion-improving conventional additive packages previously known do not necessarily pass the Currunins L 10 diesel detergency test (where a pass is defined as an average injector rating of 10.0 or less). To identify the components in the additive composition that affect injector ratings, an experimental design was earned out. A
_. ..___. _ . .~_ _ I; P-759ry synergy (i.e. a nOI11117ear (l7tCr7CtIOn~ waS ObSerVed I?etW'f:Pt7 117e OVerbaSed Ca1C111117 slllfOnatc detergent and the succinirnide dispersant. This was a surprising result which is not anticipated by any prior art.
The results of the experimental design were used to generate a model for average injector rating, as follows:
Rating = -0.159x + 0.243y - 0.0143xy + 18.4 ( 1 ) where x = concentration of succinil7ude (in pounds per thousand barrels, or PTB) y = concentration of overbased calcium sulfonate (in P'fB) Since the average injector rating must be 10.0 or lower for a pass in the Cummins L.10 test, the equation becomes:
10.0 > -0.159x + 0.243y - 0.0143xy + I 8.4 (2) or -0.159x + 0.243y - 0.0143xy <_ -8.4 (3) IS The detergent/dispersant synergy is represented by the xy term.
The model was validated by the testing of three new formulations that satisfy the above equation:
1. x = 28 PTB, y = 32 P~rB
2. x = 26 PTB, y = 40 PTB
3. x = 25 PTB, y = 48 PTB
All three formulations gave an average injector rating of below 10.0, in accordance with the model. Of course, there are an infinite number of solutions for x and y in equation 3. Examples of currently practical solutions are the following ranges:
S

x = 20-35, preferably 25-30 y = 10-120, preferably ~0-50 The amount of organometallic manganese compound was shown to have no significant adverse effect on injector ratings and is therefore not constrained by the model represented by equation 3. As an economic matter only, the amount of manganese compound is, in an embodiment, limited to 20 PTl3 or less. The benefits derived from the inclusion of a manganese compound are not directly related to injector ratings, hut are much more prevalent in the areas of particulate emission reduction, reduced NOX and SOx, reduced hydrocarbons, improved fuel economy, and combustion improvement_ Co Especially useful herein is rnethylcyclopentadienylmanganese tricarbonyl (MMT~) as the organometallic manganese compound, a succinimide prepared from 850 to 2100-MW
PIBSA and a polyalkylene polyamine approximating tetraethylenepentamine in composition as the ashless dispersant, and an overbased calcium sulfonate of ~I~BN up to about X00 as the detergent. MMT~
is available from Ethyl Corporation, Riclunond, VA. 'Ihe diesel fuel used in the Cummins L10 study was a high-sulfur (0.4wgt % sulfur) fuel, but any diesel fuel (including low-sulfur and ultralow-sulfur fuels) may be used: A separate LIO experiment has shown that the addition of 2-ethylhexyl nitrate cetane impraver to a fuel containing the inventive additive does not degrade the detergent performance.
The following examples further illustrate aspects of the present invention but do not limit 2o the present invention.
EXAMPLES:
Since the Cummins L10 test was designed to evaluate additives and fuels for on-road use in North America, HiTEC~-4080 Fuel Additive was used in this example. This additive is Ethyl Corporation's antifoam-free Greenbum u0 road diesel fuel additive package.
used with a recommended treat rate of 500 ppm (w/w). 'fhe formulation is shown in 'liable 1.
Component % weight ppm COIIIpOtlentPTB component at 500 ppm at X00 ppm total total HiTEC~ 9645 15_34 76.7 22.8 2-ethylhexanol 46.22 23l . I 68.8 Hi'CEC~ 61 I 32.16 160.8 47.9 HiTEC~ 536 0.93 4.7 1.4 D-5 021 0. 97 4. 9 1. 5 HiTEC~ 3062 4.38 21.9 6.6 Table 1. Composition of I~iTEC Iz 4080 For the purposes of this example, the European components D-5021 (demulsifier) and HiTEC~ 536 (corrosion inhibitar) were replaced with the North ~mcrican components Tolad 9310 and 50% dodecenylsuccinic acid, respectively, on an eduivalent weight basis. These components were held constant at the above concentrations in e~~ery test. The components to expected to have significant effects on Cummins L10 ratings were I-IiTEC~
9645 (a succinimide-based dispersant), HiTEC~ 611 (overbased calcium sulfonate) and I-IiTEC~ 3062 (62% MMT~ in aromatic solvent).
The resulting two-level, three-factor (23) design is shown in Figure I; the numbers along the axes denote concentrations in PTB.
t5 i?. P-7599 48 B+
H-611 C+ 6.6 a rs- ~.- a A- H-9645 A+

Figure 1. Experimental design for IIi'fECCi> 4080 components All tests were carried out in the same Cummins L,10 engine anti in the same batch of high-sulfur Cat 1K fuel. The test order was randomized. 'fhe results are shown in Table 2.
Test no. PTB H-9645PTB EI-61PTB EI-3062Avg. flow Avg. CRC
I

_ loss (%) rating D102-97-1 0 0 6.6 3.2 19.1 D102-98-1 23 0 0 4.2 14.7 D I 02-99-123 0 6.6 2.9 15.3 D102-100-I23 48 0 2.3 9.9 D102-I01-I0 48 6.6 8.9 34.7 ~

D I 02-102-111.5 24 3.3 4.1 16.8 D102-103-10 48 0 4.0 25.9 DI02-104-123 48 6.6 3.1 11.9 ~

D i 02-105-10 0 0 1.9 18.2 Table 2. Cummins L10 results for H-4080 experimental design An analysis of variance (ANOVA) on the data in Table 2 showed that average flow loss was io independent of all three factors. The ANOVA for CRC rating is shown below.
Analysis of Variance for CRC
s Source Sum of Squares Df Wean Square F-Ratio P-Value A (I-I-9645) 265.651 I 265.651 29.81 0.0028 B (I-1-G 28.6012 I 28.5012 3.20 0.1337 11 ) AB 124.031 1 124.031 13.92 0.0136 Total error 44.5563 5 8.91125 Total {corn) 462.74 8 R-squared = 90.3712 percent R-squared (adjusted for d.f,) = 84.5939 percent Standard Error of Est. = 2.98517 Mean absolute error = 1.55556 Durbin-Watson statistic = 2.10796 Iii'CEC~ 3062 and the higher-order terms AC, BC and ABC were significant at less than the 85% confidence level and are therefore excluded. 'the model coefficients are as follows:
Regression coeffs.
for CRC

______________________________________________________________________ constant = 18.4375 A {H-9645) _ -0.158696 B (H-G 1 = 0.242708 i ) AB = -0.0142663 The regression coefficients show that HiTEC~ 9645 unexpectedly decreases the CRC
response (a beneficial effect, since lower CRC ratings indicate less injector depositing), while HiTEC~ 61 I increases the ratings. 'flrere is a significant negative interaction between HiTEC~
9645 and I-IiTEC~ 611, meaning that the deleterious effect of 1-IiTEC~ 611 on CRC rating at low concentrations of dispersant is more than cancelled out at high dispersant concentrations. In other words, HiTEC~ 611 improves CRC ratings when in the presence of high amounts of HiTEC~ 9645. This effect is shown graphically by the interaction diagram in Figure 2.
Ordinarily, a p-value of 0.13 would result in HiTEC~ 611 alone being excluded from the model:
this value indicates that the coefficient is different from zero only at the 87% confidence level.

>._ ~:~.: .-nn~~.~.~.~--. ~.~ _._.._ ~_..~.._ _ . . .~.. _ .----However, if the model contains an interaction between Ivi'I'I:C~ c)645 and I-li'rEC~ 61 I, the I-IiTEC~ 61 1 term should also be included to preserve model hierarchy.
34.7 A 30.6 c t a 26.4 a 22.3 C
R
C 18.2 14.0 9.9 A- A+
Figure 2. Interaction of A:H-9645 and B:EI-611 t0 FORMULATION OF MODIa IED DISPERSANT PACKAGES TO PASS THE CUMMINS

From the model developed above, it is therefore possible to adjust the components in, for example, HiTEC~ 4080 in order to hit a desired CRC target. As mentioned previously, the maximum CRC rating for a Cummins L 10 pass is I0Ø Constant response curves for CRC as a function of HiTEC~ 9645 and HiTEC~ 611 concentrations (in PTB) are shown in Figure 3.
i0 .. ., .x .srrac,r.v~.-~. ., ~ n... n.. .~..,..- .-_--. , ._.,_..... .... ._ , x" ~,~r ~.~,~.~",.~,. ,.~".,....._- . .._.,.......
_..,..._.,.,._:,.."..,.....__- _._,.._."."."",.~nj,,~,"n. ~~.L, C'RC
__ 9 0 _.... X0.0 CIO
Figure 3. Contours of estimated response surfaces for CI2C rating Based on the above model for CRC, any combination of I-li'CECOO 9645 and HiTEC

to the right of the 10.0 contour (the dashed line) in Figure 3 should give a passing Cummins I,10 rating. 'Chree points were selected on t:he 9.0 contour (the solid line) in the L10 test. The additive combinations corresponding to these points were:
1. 28 PTB 1-Ii'rEC~ 9645 + 32 fTB 1-IiTEC~ 611 Io 2. 26 PTB HiTEC~ 9645 + 40 PTB HiTEC~ 611 3. 25 PTB HiTEC~ 9645 + 48 PTB HiTEC~ 61 I
All three packages also contained 6.6 PTB of Ethyl's MMT~ as I-IiTEC~ 3062 plus solvent, demulsifier and corrosion inhibitor as described above. The resulting Cummins L10 data are shown in Table 3.
Modified package Test no. Avg_flow loss Avg. CRC rating (%) 1 D 102-x 07-2 2.0 8.6 2 D 102-107-1 3.1 8.5 3 D 102-109- i 3.3 9.9 Table 3. Cummins L10 results for modified versions of H1TEC~ 4080 As expected from the above model and calculations, all three packages pass the Cummins L10 test.
A simple 23 experimental design has determined the quantitative effects of various components in a Greenburn~ Diesel Fuel Additive package on Cummins L 10 performance. It II
,____ .,r ,~~. ""K. . ....~. ~._,.~x.T..., ........ _.. "~x~,~,"_y:_=
,;,~i,~,.~,v,~~,A,.,.. . ...~ ._._.~,~~m~,-. __._ ._. . __..._.____ _._~___.... ___._....____ . . ~ ~ . .. _ .. ~. .~...

Et'-?599 was found that the succinimide dispersant (lfiT'EC~ 9645) had a beneficial effect on injector ratings, while the overbased calcium sulfonate detergent (1-Ii'fI;C~ 61 1) harmed those ratings. In addition, a strong interaction between these two components was observed which reduced the undesirable effect of the detergent. MMTC~ (as HiTEC~ 3062) had no significant effect on injector cleanliness. The model derived from the experimental design w<is used to formulate modified Greenburn 0-type packages that passed the Cummins LIO test.
Other embodiments of the present invention will be apparent to those skilled in the art from consideration of the spe<:ification and practice of the invention disclosed herein. As used throughout the specification and claims, "a" and/or "an'' may refer to one or more than one.
t0 Unless otherwise indicated, all numbers expressing quantities of in~;redients, properties such as molecular weight, percent, ratio, reaction conditions. and so forth used in the specification and claims are to be understood as being modified in all instances by the term "about." Accordingly, unless indicated to the contrary, the numerical parameters set forth in the specification and claims are approximations flat may vary depending upon the desired properties sought to be i5 obtained by the present invention. At the very least, and not as an attempt to limit the application of the doctrine of equivalents to the scope of the claims, each numerical parameter should at least be construed in light of the number of reported significant digits and by applying ordinary rounding techniques. Notwithstanding that the numerical ranges and parameters setting forth the broad scope of the invention are approximations, the numerical values set forth in the specific 2o examples are reported as precisely as possible. Any nurner~ical value, however, inherently contains certain errors necessarily resulting from the standard deviation found in their respective testing measurements. It is intended that the specification and examples be considered as _. . . . ~ ~ ..~.. v ,. ,~~.»"~.w. , .., " '. ,~.,......_ __ ~.~,~,~ » , 4~~",.,~. _. .,..~.,m~._.._. ....._... ~.. ,h .".mw.._. __~,. ,~~.~
~.~,..,~~,..."~a~,e~.

exemplary only, with a true scope and spirit of the invention being indicated by the following claims.

Claims (12)

1. A distillate fuel additive composition comprising an organometallic manganese compound, an alkyl-substituted succinimide ashless dispersant, and an overbased calcium sulfonate detergent.
2. The fuel additive of claim 1 wherein the organometallic manganese compound comprises methylcyclopentadienylmanganese tricarbonyl.
3. The fuel additive of claim 1 wherein the succinimide is prepared from polyisobutylene succinic anhydride and a polyalkylene polyamine.
4. The fuel additive of claim 1 wherein the succinimide is prepared from polyisobutylene succinic anhydride and tetraethylenepentamine.
5. The fuel additive of claim 1 wherein the polyisobutylene of the alkyl-substituted succinimide is prepared from about 850 to 2100 molecular weight polyisobutylene.
6. The fuel additive of claim 1 wherein the polyisobutylene of the alkyl-substituted succinimide is prepared from about 850 to 1300 molecular weight polyisobutylene.
7. The fuel additive of claim 1 wherein the polyisobutylene of the alkyl-substituted succinimide is prepared from about 950 molecular weight polyisobutylene .
8. The fuel additive of claim 1 wherein the composition comprises an organometallic complex of manganese, an overbased calcium sulfonate detergent, and an ashless alkyl-substituted succinimide dispersant such that when the additive composition is dissolved in a distillate fuel, the following relationship is satisfied:
-0.159x + 0.243y - 0.0143xy <= -8.4 where x = concentration of succinimide (in pounds per thousand barrels) y = concentration of overbased calcium sulfonate (in PTB) with the following limitations:

x = 20-35, and y = 10-120.
9. The fuel additive of claim 1 wherein tile overbased calcium sulfonate has a TBN of above about 200.
10. The fuel additive of claim 1 wherein the overbased calcium sulfonate has a TBN of about 300.
11. A fuel comprising a major amount of a middle distillate fuel and a minor amount of a fuel additive composition comprising an organometallic manganese compound, an alkyl-substituted succinimide ashless dispersant, and an overbased calcium sulfonate detergent of TBN about 300.
12. A method for improving the cleanliness of a fuel intake systems by use in the fuel intake system of a fuel containing a distillate fuel additive composition comprising an organometallic manganese compound, an alkyl-substituted succinimide ashless dispersant, and an overbased calcium sulfonate detergent of TBN about 300.
CA002469766A 2003-07-08 2004-06-04 Distillate fuel compositions for improved combustion and engine cleanliness Abandoned CA2469766A1 (en)

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US10/614,771 US20050005506A1 (en) 2003-07-08 2003-07-08 Distillate fuel compositions for improved combustion and engine cleanliness

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CN1576353A (en) 2005-02-09
CN100506955C (en) 2009-07-01
EP1496100A1 (en) 2005-01-12
US20050005506A1 (en) 2005-01-13
SG108978A1 (en) 2005-02-28
JP2005029796A (en) 2005-02-03

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