Field of the Invention
[0001] The present invention relates to the use of a fuel additive for protecting and improving
operation of combustion exhaust after treatment systems. The additive contains one
or more manganese compounds. The additive can be introduced into a combustion chamber
as part of the fuel, or it may be injected alone or with the fuel into the combustion
exhaust. The additive will then enhance the operation of after treatment systems including,
for example, those that incorporate catalyzed and continuously regenerating technology
diesel particulate filters.
Description of the Prior Art
[0002] It is well known in the automobile industry, or any industry where hydrocarbonaceous
fuels are burned, to reduce tailpipe (or smokestack) emissions by using various strategies.
For example, the most common method for reducing emissions from spark ignition engines
is by careful control of the air-fuel ratio and ignition timing. Retarding ignition
timing from the best efficiency setting reduces HC and NO
x emissions, while excessive retard of ignition increases the output of CO and HC.
Increasing engine speed reduces HC emissions, but NO
x emissions increase with load. Increasing coolant temperature tends to reduce HC emissions,
but this results in an increase in NO
x emissions.
[0003] It is also known that treating the effluent stream from a combustion process by exhaust
after treatment can lower emissions. The effluent contains a wide variety of chemical
species and compounds, some of which may be converted by a catalyst into other compounds
or species. For example, it is known to provide exhaust after treatment using a three-way
catalyst and a lean NO
x trap. Other catalytic and non-catalytic methods are also known.
[0004] Thermal reactors are noncatalytic devices which rely on homogeneous bulk gas reactions
to oxidize CO and HC. However, in thermal reactors, NO
x is largely unaffected. Reactions are enhanced by increasing exhaust temperature (e.g.
by a reduced compression ratio or retarded timing) or by increasing exhaust combustibles
(rich mixtures). Typically, temperatures of 1500
oF (800 °C) or more are required for peak efficiency. Usually, the engine is run rich
to give 1 percent CO and air is injected into the exhaust. Thermal reactors are seldom
used, as the required setting dramatically reduces fuel efficiency.
[0005] Catalytic systems are capable of reducing NO
x as well as oxidizing CO and HC. However, a reducing environment for NO
x treatment is required which necessitates a richer than chemically correct engine
air-fuel ratio. A two-bed converter may be used in which air is injected into the
second stage to oxidize CO and HC. While efficient, this procedure results in lower
fuel economy.
[0006] Single stage, three way catalysts (TWC's) are widely used, but they require extremely
precise fuel control to be effective. Only in the close proximity of the stoichiometric
ratio is the efficiency high for all three pollutants, excursions to either side of
stoichiometric can cause increases in hydrocarbon and carbon monoxide or NOx emissions.
Such TWC systems can employ, for example, either a zirconia or titanium oxide exhaust
oxygen sensor or other type of exhaust sensor and a feedback electronic controls system
to maintain the required air-fuel ratio near stoichiometric.
[0007] Catalyst support beds may be pellet or honeycomb (e.g. monolithic). Suitable reducing
materials include ruthenium and rhodium, while oxidizing materials include cerium,
platinum and palladium.
[0008] Diesel systems raise a different set of challenges for emissions control. Strategies
for reducing particulate and HC include optimizing fuel injection and air motion,
effective fuel atomization at varying loads, control of timing of fuel injection,
minimization of parasitic losses in combustion chambers, low sac volume or valve cover
orifice nozzles for direct injection, reducing lubrication oil contributions, and
rapid engine warm-up.
[0009] In terms of after treatment, it is known that diesel engines generally burn lean
and the exhaust will therefore usually contain excess oxygen. Thus, NO
x reduction with conventional three-way catalysts is not feasible. NO
x is removed from diesel exhaust by either selective catalytic reduction, the use of
lean NOx catalysts such as those comprised of zeolitic catalysts or using metals such
as iridium, or catalyzed thermal decomposition of NO into O
2 and N
2.
[0010] Diesel particulate traps such as catalyzed diesel particulate filters (C-DPFs) and
continuously regenerating technology diesel particulate filters (CRT-DPFs) have been
developed which employ ceramic or metal filters. Thermal and catalytic regeneration
can burn out the material stored. New particulate standards currently under review
may necessitate such traps. Fuel composition, including sulfur and aromatic content,
and the burning of lubricant can contribute to increased particulate emissions. Catalysts
have been developed for diesels which are very effective in oxidizing the organic
portion of the particulate.
[0011] Improved fuel economy can be obtained by using a lean-burn gasoline engine, for example,
a direct injection gasoline engine, however currently NO
x cannot be reduced effectively from oxidizing exhaust using a typical three-way catalyst
because the high levels of oxygen suppress the necessary reducing reactions. Without
a NO
x adsorber or lean NO
x trap (LNT), the superior fuel economy of the lean-burn gasoline engine cannot be
exploited. The function of the LNT is to scavenge the NO
x from the exhaust, retaining it for reduction at some later time. Periodically, the
LNT must be regenerated by reducing the NO
x. This can be accomplished by operating the engine under rich air-fuel ratios for
the purpose of purging the trap. This change in operating conditions can adversely
effect fuel economy as well as driveability. These LNT's may also be placed on diesel
engines, which also operate in a lean air-fuel mode. As in the lean-burn gasoline
engines, the exhaust of both types of engines is net oxidizing and therefore is not
conducive to the reducing reactions necessary to remove NO
x. It is an object of the present invention to improve the storage efficiency and durability
of the LNT and to prolong the useful life of the LNT before regeneration is necessary.
[0012] It is well known that NO
x adsorbers are highly vulnerable to deactivation by sulfur (see, for example, M. Guyon
et al.,
Impact of Sulfur on NOx Trap Catalyst Activity-Study of the Regeneration Conditions, SAE Paper No. 982607 (1998); and P. Eastwood,
Critical Topics in Exhaust Gas Aftertreatment, Research Studies Press Ltd. (2000) pp.215-218.) and other products resulting from
fuel combustion and normal lubricant consumption. It is an object of the present invention
to provide fuel or lubricant compositions capable of reducing the adverse impact of
sulfur, and other exhaust byproducts, on the emissions system including NO
x adsorbers and LNTs.
[0013] Performance fuels for varied applications and engine requirements are known for controlling
combustion chamber and intake valve deposits, cleaning port fuel injectors and carburetors,
protecting against wear and oxidation, improving lubricity and emissions performance,
and ensuring storage stability and cold weather flow. Fuel detergents, dispersants,
corrosion inhibitors, stabilizers, oxidation preventers, and performance additives
are known to increase desirable properties of fuels.
[0014] Organometallic manganese compounds, for example methylcyclopentadienyl manganese
tricarbonyl (MMT®), available from Ethyl Corporation of Richmond, Virginia, are known
for use in gasoline as both emissions-reducing agents and as antiknock agent (see,
e.g. U.S. Patent 2,818,4I7). These manganese compounds have been used to lower deposit
formation in fuel induction systems (U.S. Patents 5,551,957 and 5,679,116), sparkplugs
(U.S. Patent 4,674,447) and in exhaust systems (U.S. Patents 4,175,927; 4,266,946;
4,317,657, and 4,390345). Organometallic iron compounds, such as ferrocene, are known
as well for octane enhancement (U.S. Patent 4,139,349).
[0015] Organometallics for example compounds of Ce, Pt, Mn or Fe among others have been
added to fuel to enhance the ability of particulate traps to regenerate or to directly
reduce the emissions of particulate from diesel or compression ignition type engines
or other combustion systems. These additives function through the action of the metal
particles that are the product of additive breakdown on the particulate matter during
combustion or in the exhaust or particulate trap.
Summary of the Invention
[0016] Accordingly, it is an object of the present invention to overcome the limitations
and drawbacks of the foregoing systems and methods to provide methods for using a
composition to protect and improve the operation of combustion exhaust after treatment
systems.
[0017] In one embodiment, a method of enhancing the operation of an emission after treatment
system in a diesel fuel combustion system includes supplying a diesel fuel comprising
an additive that includes a manganese compound to a diesel fuel combustion system.
The combustion system comprises a catalyzed or, alternatively, continuously regenerating
technology diesel particulate filter. The fuel is then combusted in the combustion
chamber to produce at least one byproduct comprising the manganese compound. The manganese
is in an effective amount to complex with the at least one combustion byproduct. The
manganese compound or manganese ion may be an inorganic metal compound or an organometallic
compound. The inorganic metal compound can be selected from the group consisting of
fluorides, chlorides, bromides, iodides, oxides, nitrates, sulfates, phosphates, carbonates,
hydrides, hydroxides, nitrides, and mixtures thereof. The organometallic compound
is selected from the group consisting of alcohols, aldehydes, ketones, esters, anhydrides,
sulfonates, phosphonates, chelates, phenates, crown ethers, carboxylic acids, amides,
acetyl acetonates, and mixtures thereof. A preferred organometallic compound is manganese
methylcyclopentadienyl tricarbonyl.
[0018] In a still further embodiment, a method of enhancing the operation of an emissions
after treatment system in a diesel fuel combustion system comprises supplying a diesel
fuel to a diesel fuel combustion system. The combustion system may comprise a catalyzed
diesel particulate filter or a continuously regenerating technology diesel particulate
filter. The fuel is combusted in a combustion system to produce at least one combustion
byproduct in an exhaust stream. An additive comprising a manganese compound is injected
into the exhaust stream. The manganese compound complexes with at least one combustion
byproduct. The manganese compound which can be an inorganic or organometallic compound
is supplied in an effective amount to complex with the at least one combustion byproduct.
The inorganic metal compound or organometallic compound may be as noted earlier herein.
[0019] In a still further embodiment, an emissions control system for the after treatment
of a diesel fuel combustion process exhaust stream comprises an exhaust passageway.
The exhaust passageway allows for passage of an exhaust stream containing exhaust
byproducts from the combustion of a diesel fuel comprising a manganese compound. This
system also includes a catalyzed or continuously regenerating technology diesel particulate
filter located within the exhaust passageway and adapted to contact the exhaust stream.
The exhaust stream comprises a manganese compound which complexes with at least one
of the exhaust byproducts. The alternatives of possible manganese compounds include
those noted herein.
[0020] In a still further embodiment, an emission control system for the after treatment
of a diesel fuel combustion process exhaust stream includes an exhaust passageway.
The exhaust passageway for the passage of an exhaust stream contains exhaust byproducts
from the combustion of a diesel fuel. A catalyzed or continuously regenerating technology
diesel particulate filter is located within the exhaust passageway and is adapted
to contact the exhaust stream. The exhaust stream has an additive introduced into
it, the additive comprising a manganese compound which complexes with at least one
of the exhaust byproducts. The alternatives of possible manganese compounds include
those noted herein.
[0021] In a still further embodiment, a method of enhancing the operation of an emission
after treatment system in a combustion system includes supplying a fuel comprising
an additive that includes a manganese compound to a fuel combustion system. The fuel
is then combusted in the combustion chamber to produce at least one byproduct comprising
the manganese compound. The manganese is in an effective amount to complex with the
at least one combustion byproduct.
[0022] In a still further embodiment, a method of enhancing the operation of an emissions
after treatment system in a combustion system comprises supplying a fuel to a combustion
system. The fuel is combusted in a combustion system to produce at least one combustion
byproduct in an exhaust stream. An additive comprising a manganese compound is injected
into the exhaust stream. The manganese compound complexes with at least one combustion
by product.
Detailed Description
[0023] The additives used in the methods and systems of the present invention are inorganic
or organometallic manganese containing compounds soluble in fuels. This fuel is then
combusted in a combustion system that includes an after treatment system. It protects
the after treatment system from harmful combustion byproducts that could otherwise
neutralize their effectiveness. The manganese in the additive also promotes the oxidation
of carbon particulate matter. Upon introduction into the exhaust stream, the manganese
comes into contact with the carbon fraction of the particulate, accelerates carbon
oxidation reactions, and aids in after treatment system regeneration. The manganese
compound also reduces the rate of soot accumulation. The exhaust system may also contain
other after treatment systems.
[0024] The hydrocarbonaceous fuel combustion systems that may benefit from the present invention
include all combustion engines that burn fuels. By "combustion system" herein is meant
any and all internal and external combustion devices, machines, engines, turbine engines,
boilers, incinerators, evaporative burners, stationary burners and the like which
can combust or in which can be combusted a fuel. Fuels suitable for use in the operation
of combustion systems of the present invention include diesel fuel, jet fuel, kerosene,
synthetic fuels, such as Fischer-Tropsch fuels, liquid petroleum gas, fuels derived
from coal, natural gas, propane, butane, unleaded motor and aviation gasolines, and
so-called reformulated gasolines which typically contain both hydrocarbons of the
gasoline boiling range and fuel-soluble oxygenated blending agents, such as alcohols,
ethers and other suitable oxygen-containing organic compounds. Oxygenates suitable
for use in the present invention include methanol, ethanol, isopropanol, t-butanol,
mixed C
1 to C
5 alcohols, methyl tertiary butyl ether, tertiary amyl methyl ether, ethyl tertiary
butyl ether and mixed ethers. Oxygenates, when used, will normally be present in the
base fuel in an amount below about 25% by volume, and preferably in an amount that
provides an oxygen content in the overall fuel in the range of about 0.5 to about
5 percent by volume. Other fuels that are useful in the methods and devices of the
present invention are gasoline, bunker fuel, coal dust, crude oil, refinery "bottoms"
and by-products, crude oil extracts, hazardous wastes, yard trimmings and waste, wood
chips and saw dust, agricultural waste or tillage, plastics and other organic waste
and/or by-products, and mixtures thereof, and emulsions, suspensions, and dispersions
thereof in water, alcohol, or other carrier fluids. By "diesel fuel" herein is meant
one or more fuels selected from the group consisting of diesel fuel, biodiesel, biodiesel-derived
fuel, synthetic diesel and mixtures thereof and other products meeting the definitions
of ASTM D975. It is preferred that the sulfur content of the diesel fuel be less than
100 ppm, and especially preferred that the sulfur content be less than 30 ppm. Fuels
having relatively high sulfur content, while within the scope of the present invention,
are currently impractical for use with catalytically enhanced after treatment systems.
[0025] Conventional combustion systems useful with the present invention will typically
include some degree of emission control or after treatment system. In all cases of
combustion, the emission treatment may include a catalytic system to reduce harmful
emissions. Of course, other emission treatment systems are well known. Unfortunately,
many of such emission systems have a tendency to lose their effectiveness over time
due to poisoning or degradation of emission treatment system components.
[0026] The present invention contemplates providing a manganese compound to an additive,
to a fuel composition or, alternatively, directly into the exhaust stream or combustion
zone resulting from the combustion process, whereby the operation of the emission
treatment system components will be significantly enhanced. A copending application
discloses various delivery and combination opportunities when using an aqueous, water
soluble, manganese containing additive. U.S. Patent Application Serial No. 10/ 165,462,
filed June 7, 2002.
[0027] The preferred metal herein includes elemental and ionic manganese, precursors thereof,
and mixtures of metal compounds including manganese. These manganese compounds may
be either inorganic or organic. Also effective in the present invention is the generation,
liberation or production
in situ of manganese or manganese ions.
[0028] Preferred inorganic metallic compounds in an embodiment of the present invention
can include by example and without limitation fluorides, chlorides, bromides, iodides,
oxides, nitrates, sulfates, phosphates, nitrides, hydrides, hydroxides, carbonates
and mixtures thereof. Manganese sulfates and phosphates will be operative in the present
invention and may, in certain fuels and combustion applications, not present unacceptable
additional sulfur and phosphorus combustion byproducts. Preferred organometallic compounds
in an embodiment of the present invention include alcohols, aldehydes, ketones, esters,
anhydrides, sulfonates, phosphonates, chelates, phenates, crown ethers, carboxylic
acids, amides, acetyl acetonates, and mixtures thereof.
[0029] Especially preferred manganese containing organometallic compounds are manganese
tricarbonyl compounds. Such compounds are taught, for example, in US Patent Nos. 4,568,357;
4,674,447; 5,113,803; 5,599,357; 5;944,858 and European Patent No. 466 512 B1.
[0030] Suitable manganese tricarbonyl compounds which can be used in the practice of this
invention include cyclopentadienyl manganese tricarbonyl, methylcyclopentadienyl manganese
tricarbonyl, dimethylcyclopentadienyl manganese tricarbonyl, trimethylcyclopentadienyl
manganese tricarbonyl, tetramethylcyclopentadienyl manganese tricarbonyl, pentamethylcyclopentadienyl
manganese tricarbonyl, ethylcyclopentadienyl manganese tricarbonyl, diethylcyclopentadienyl
manganese tricarbonyl, propylcyclopentadienyl manganese tricarbonyl, isopropylcyclopentadienyl
manganese tricarbonyl, tert-butylcyclopentadienyl manganese tricarbonyl, octylcyclopentadienyl
manganese tricarbonyl, dodecylcyclopentadienyl manganese tricarbonyl, ethylmethylcyclopentadienyl
manganese tricarbonyl, indenyl manganese tricarbonyl, and the like, including mixtures
of two or more such compounds. Preferred are the cyclopentadienyl manganese tricarbonyls
which are liquid at room temperature such as methylcyclopentadienyl manganese tricarbonyl,
ethylcyclopentadienyl manganese tricarbonyl, liquid mixtures of cyclopentadienyl manganese
tricarboriyl and methylcyclopentadienyl manganese tricarbonyl, mixtures of methylcyclopentadienyl
manganese tricarbonyl and ethylcyclopentadienyl manganese tricarbonyl, etc.
[0031] Preparation of such compounds is described in the literature, for example, U.S. Pat.
No. 2,818,417, the disclosure of which is incorporated herein in its entirety.
[0032] When formulating additives to be used in the methods and systems of the present invention,
the manganese compounds are employed in amounts sufficient to reduce the impact of
poisons, e.g., sulfur, lead, zinc, soot and phosphorus, on the after treatment systems,
reduce the rate of soot accumulation, reduce the temperature at which the soot oxidizes,
and otherwise generally enhance the operation of after treatment systems including,
for instance, a catalyzed diesel particulate filter, or alternatively, a continuously
regenerating technology diesel particulate filter.
[0033] Manganese compounds are believed to bind with poisons in the exhaust stream to prevent
those poisons from binding or depositing on an after treatment system such as the
catalytic surface of the diesel particulate filter. See, e.g., A. J. Nelson, J. L.
Ferreira, J. G. Reynolds, J. W. Roos and S. D. Schwab, "X-Ray Absorption Characterization
of Diesel Exhaust Particulates," Applications of Synchrotron Radiation Techniques
to Materials Science V, Materials Research Society Conference Proceedings, No. 590,
63 (2000). For instance, manganese sulfates and phosphates may be formed and are trapped
within a filter. These manganese sulfates and phosphates do not form a glaze over
or otherwise tie up catalytic sites in a filter. This mechanism is distinguished from
other additives such as platinum. Platinum compounds do not bond or otherwise complex
with poisons such as sulfates and phosphates. Instead, it is hypothesized in the literature
that platinum compounds in an additive act to replace or substitute as the catalyst
on the surface of the filter. It is basic chemical differences such as those described
herein that distinguish manganese from other metals like platinum. In formulating
additives for use in the present invention, therefore, it is important that effective
amounts of manganese be employed, and further that any other metal compounds that
can be additionally incorporated must not have any negative effects on the manganese
mechanisms.
[0034] The amount or concentration of the additive may be selected based on the concentration
of sulfur in the diesel fuel. A preferred treatment rate of the manganese compound
can be in excess of 100 mg of manganese/ liter, more preferably up to about 50mg/liter,
and most preferably about 1 to about 30mg/ liter.
[0035] The term "after treatment system" is used throughout this application to mean any
system, device, method, or combination thereof that acts on the exhaust stream or
emissions resulting from the combustion of a diesel fuel. "After treatment systems"
include all types of diesel particulate filters - - catalyzed and uncatalyzed, lean
NO
× traps and catalysts, select catalyst reduction systems, SO
x traps, diesel oxidation catalysts, mufflers, NO
x sensors, oxygen sensors, temperature sensors, backpressure sensors, soot or particulate
sensors, state of the exhaust monitors and sensors, and any other types of related
systems and methods.
[0036] There are multiple types of diesel particulate filters (DPFs). Conventional, uncatalyzed
DPFs are a well-known technology that has been used for many years. In operation,
combustion byproducts such as particulates and soot are trapped and then oxidized,
or "burned off". "Catalyzed diesel particulate filters" (C-DPFs) are filters incorporating
a catalyst on or within the filter substrate that are adapted to reduce the oxidation
temperature of the combustion byproducts captured in the filter. C-DPFs currently
include cordierite or silicon carbide monolithic type filters. A "continuously regenerating
technology diesel particulate filter" (CRT-DPF) is a system where the catalyst is
a separate, flow-through substrate that precedes the diesel particulate filter in
the exhaust passageway.
[0037] Diesel fuels, when combusted in engines operating under the diesel cycle, emit unburned
soot particles into the exhaust gas stream. Because the oxidation temperature of soot
is in excess of 500°C, it is desirable to employ catalysts either within or preceding
the filters to lower the soot oxidation temperature. A catalyst that is part of the
filter substrate, i.e., a catalyzed diesel particulate filter, or C-DPF, requires
an exhaust temperature between 325 and 400°C to initiate filter regeneration. Regeneration
is the oxidation of accumulated soot. In this system, the soot accumulates on the
catalytic sites within the filter substrate and the combination of temperature, pressure
and the presence of the catalyst lower the temperature required for regeneration.
In a continuously regenerating technology diesel particulate filter, soot oxidation
temperature is reduced because the catalyst oxidizes NO in the exhaust gas to NO
2. The increased level of NO
2 promotes an increased level of soot oxidation within the filter.
[0038] The terms "complex" or "complexing" are intended herein to describe the combination
of or reaction by the manganese containing compound with the combustion byproduct(s)
such as poisons, soot and other particulates. The combination includes covalent or
ionic reactions or any other binding of the metal compound with the combustion byproduct.
Further, the term "combustion byproduct" includes, but is not limited to, particulates,
soot, unburned soot, uncombusted hydrocarbons, partially-combusted hydrocarbons, combusted
hydrocarbons, oxides of nitrogen, and any other gas, vapor, particle or compound that
results from the combustion of a fuel.
[0039] Reference is also made throughout of the term "enhanced" in the context of operation
of an emissions after treatment system. The term "enhanced" means an improvement in
the operation of an after treatment system relative to the operation of a similar
system that does not have a manganese compound combusted or injected or otherwise
streamed through it. "Enhanced" operation includes, but is not limited to, reduction
in the impact of poisons on the emissions control system, reduction in the rate of
soot accumulation, and reduction in the temperature at which the soot is oxidized
in the filter.
[0040] When the emissions system contains a component which is poisonable by combustion
byproducts (such as those containing sulfur, phosphorus, lead, zinc or soot), for
instance, a barium-containing lean NO
x trap, the present invention provides novel methods for providing a substance which
competes with the active site (e.g., barium) in the lean-burning exhaust. As long
as the manganese containing compound of the additive will compete with the metal of
the catalyst system for complexing with the potential emissions system poisons (e.g.,
sulfur) the manganese may be suitable for use as scavenging agents. Further, the manganese
scavengers of the present invention can reduce the detrimental impact of other poisons
such as sulfur, phosphorus, lead, zinc, or soot on emissions control systems of the
lean burn combustion systems in one embodiment of the present invention.
[0041] In this invention, when the manganese containing, fuel-borne catalyst was used in
combination with the CRT-DPF, there was an unanticipated benefit. There is a lower
soot accumulation rate within the CRT-DPF and the regeneration temperature is reduced
below the regeneration temperature observed with either the fuel-borne catalyst or
CRT-DPF alone.
Example 1
[0042] The additives useful herein are organometallic, manganese containing compounds soluble
or dispersible in diesel fuel. The manganese promotes the oxidation of carbon particulate
matter. The exhaust gas after treatment device is a continuously regenerating technology
diesel particulate filter (CRT-DPF). Upon introduction of the fuel into the combustion
chamber or exhaust stream, the manganese is released and combines or complexes with
the carbon fraction of the particulate matter, accelerating the oxidation reactions
that take place prior to and during accumulation within the CRT-DPF. The measure of
soot loading within a filter is the increase in exhaust gas backpressure (EGBP). A
comparison of EGBP profiles during base and additized fuel soot loading tests are
shown in Figures 1 and 2. Figure 1 displays the initial soot accumulation profile
prior to catalyst light-off, and shows that use of the additized fuel leads to an
immediate benefit of reduced EGBP. The continuation of this benefit through 10 hours
is displayed in Figure 2. The soot accumulation rate for base fuel, as measured by
EGBP increase, is 0.06 kPa per hour. When additized fuel is tested, the rate is reduced
by a factor of three to 0.02 kPa per hour. More details regarding this testing described
herein is contained in SAE Paper No. 2002-01-2728, "The Role That Methylcyclopentodienyl
Manganese Tricarbonyl (MMT) Can Play in Improving Low-Temperature Performance of Diesel
Particulate Filters" which is incorporated herein in its entirety.
[0043] The base fuel used in this example was an ultra-low sulfur diesel fuel obtained from
Phillips. This fuel had a nominal sulfur level of 3 ppm. The additive was provided
so that the additized fuel had 20 mgMn/liter. The additive used was MMT® (Ethyl Corporation).
[0044] After filters are loaded with soot, it is useful to examine the temperature where
regeneration (the burning-off of accumulated soot) will occur.. Figure 3 shows the
results of regeneration tests when base fuels and additized fuels are burned. With
unadditized fuel, filter regeneration was not observed at temperatures exceeding 380°C.
With additized fuel, regeneration begins when exhaust temperature exceeds approximately
280°C. The accumulated carbon within the filter combusts, leading to complete filter
regeneration. Notably, once the soot is burned off, the engine backpressure remains
below that amount of backpressure seen with the unadditized fuel. In other words,
not only does the soot burn off at a lower temperature with the additized fuel, the
backpressure remains lower than with unadditized fuel as shown in Figure 3.
Example 2
[0045] The exhaust gas after treatment device is a catalyzed diesel particulate filter (C-DPF).
Upon introduction of the additized fuel into the combustion chamber or exhaust stream,
the manganese is released and combines with the carbon fraction of the particulate
matter, accelerating the oxidation reactions that take place prior to and during accumulation
within the C-DPF. Because the rate of soot accumulation is lower and the soot contains
a catalyst metal, the regeneration temperature is reduced relative to what would be
expected with the C-DPF and unadditized fuel.
Example 3
[0046] In the applications described in Examples 1 and 2, the manganese used will form stable
metal complexes including manganese phosphates. A portion of the manganese released
into the combustion chamber or exhaust interacts with lubricant-derived phosphorus
to form the stable metal phosphates as solid particulate and this reduces or prevents
phosphorus deposition on the catalyst metal employed in the CRT-DPF, or the C-DPF.
The use of these manganese containing fuel additives will protect the catalyst from
deterioration resulting from phosphorus poisoning.
Example 4
[0047] In the applications described in Examples 1 and 2, the manganese additive used is
one that will also form stable metal sulfates. The CRT-DPF or C-DPF is followed by
a lean-NOx storage device that is sensitive to sulfur poisoning. A portion of the
metal released into the combustion chamber or exhaust interacts with either fuel or
lubricant-derived sulfur to form stable manganese sulfates, thereby scavenging the
SO
2 and SO
3 and reducing or preventing deposition of sulfur species on the lean-NOx storage device.
Example 5
[0048] The manganese containing additives of the present invention enhance operation of
an after treatment system by reducing the sintering of combustion byproduct metal
on the surface of the DPF. The sintering of combustion byproduct metals may cover
and render ineffective catalyst sites on the surface of the catalyzed DPF. "Sintering"
is the fusion of combustion byproduct particles on the filter surfaces as a result
of the heat in that filter. The manganese containing additive reduces the amount of
sintering on the filter surfaces, as compared to the amount of sintering when unadditized
fuel is burned, and therefore increases the effective life of the filter. It also
makes the filter easier to clean because of the reduced sintering of the byproducts
to the walls of the filter.
Example 6
[0049] The manganese containing additives of the present invention enhance operation of
an after treatment system by accelerating ash buildup in a DPF but nevertheless reducing
rate of backpressure increase. The manganese binds with combustion byproducts, e.g.,
sulfur and phosphorous oxides, and forms stable manganese compounds that are then
trapped as and with the ash in the filter. Surprisingly, it has been discovered that
this literal increase in ash does not increase backpressure. Further, by using a manganese
containing additive, the DPF will need to be cleaned less often and the ash can be
more completely removed when it is cleaned.
[0050] It is to be understood that the reactants and components referred to by chemical
name anywhere in the specification or claims hereof, whether referred to in the singular
or plural, are identified as they exist prior to coming into contact with another
substance referred to by chemical name or chemical type (e.g., base fuel, solvent,
etc.). It matters not what chemical changes, transformations and/or reactions, if
any, take place in the resulting mixture or solution or reaction medium as such changes,
transformations and/or reactions are the natural result of bringing the specified
reactants and/or components together under the conditions called for pursuant to this
disclosure. Thus the reactants and components are identified as ingredients to be
brought together either in performing a desired chemical reaction (such as formation
of the organometallic compound) or in forming a desired composition (such as an additive
concentrate or additized fuel blend). It will also be recognized that the additive
components can be added or blended into or with the base fuels individually per se
and/or as components used in forming preformed additive combinations and/or sub-combinations.
Accordingly, even though the claims hereinafter may refer to substances, components
and/or ingredients in the present tense ("comprises", "is", etc.), the reference is
to the substance, components or ingredient as it existed at the time just before it
was first blended or mixed with one or more other substances, components and/or ingredients
in accordance with the present disclosure. The fact that the substance, components
or ingredient may have lost its original identity through a chemical reaction or transformation
during the course of such blending or mixing operations or immediately thereafter
is thus wholly immaterial for an accurate understanding and appreciation of this disclosure
and the claims thereof.
[0051] At numerous places throughout this specification, reference has been made to a number
of U.S. Patents, published foreign patent applications and published technical papers.
All such cited documents are expressly incorporated in full into this disclosure as
if fully set forth herein.
[0052] This invention is susceptible to considerable variation in its practice. Therefore
the foregoing description is not intended to limit, and should not be construed as
limiting, the invention to the particular exemplifications presented hereinabove.
Rather, what is intended to be covered is as set forth in the ensuing claims and the
equivalents thereof permitted as a matter of law.
[0053] Patentee does not intend to dedicate any disclosed embodiments to the public, and
to the extent any disclosed modifications or alterations may not literally fall within
the scope of the claims, they are considered to be part of the invention under the
doctrine of equivalents.