nanolubricantsfordieselengines:related emissions and compatibility

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  • 7/26/2019 Nanolubricantsfordieselengines:Related emissions and compatibility

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    Nanolubricants for diesel engines: Related emissions and compatibility

    with the after-treatment catalysts

    S.J. Castillo Marcano, S. Bensaid, F.A. Deorsola, N. Russo, D. Fino n

    Politecnico di Torino, Department of Applied Science and Technology, Corso Duca degli Abruzzi 24, 10129 Torino, Italy

    a r t i c l e i n f o

    Article history:

    Received 23 July 2013

    Received in revised form10 October 2013

    Accepted 17 October 2013Available online 1 November 2013

    Keywords:

    Lubricants

    Diesel engine

    Molybdenum disulde

    After-treatment catalysts

    a b s t r a c t

    The effect of the lubricant oil additivated with MoS2 nanopowders was assessed through a set of full-

    scale tests on a real diesel engine several engine points and cooling water temperatures were

    investigated for both a reference oil and a MoS2-additivated one. The emission abetment efciency of theDOC and DPF reduces the gas and solid pollutants obtained with the MoS 2-additivated oil to levels

    equivalent to the ones reached with the reference oil. An endurance test of 100 h (equivalent to

    10,000 km) proved the stability of the catalytic system and the suitability of commercial after-treatment

    catalysts to cope with the emission modications induced by the inclusion of nanoadditives in the oil

    matrix.

    & 2013 Elsevier Ltd. All rights reserved.

    1. Introduction

    Fluid lubricants are used in almost every eld of human

    technological activity and their purpose is multi-fold they reducefrictional resistance, protect the contacting surfaces of engines

    against wear, remove wear debris, reduce heat and contribute to

    cooling, improve fuel economy and reduce emissions.

    Advanced nanomaterials have shown some promise because of

    their contribution to reducing friction and enhancing protection

    against wear[13]. When incorporated in full lubricant formula-

    tions in a stable way, and if their performance benets can be

    sustained under those circumstances, they offer the possibility of

    some performance breakthroughs which have not been witnessed

    since the development of the now ubiquitous anti-wear additives,

    zinc dialkyl dithiophosphate (ZDDP) and molybdenum dithiocar-

    bamate (MoDTC). It has been demonstrated that ZDDP and MoDTC

    used together improve the friction and anti-wear performances by

    the formation of a molybdenum disul

    de layer on the rubbingsurfaces [46]. The developments brought by nanomaterials can

    contribute to a substantial energy saving, reduce equipment

    maintenance and lengthen the life of the machines. In the case

    of engine oil (crankcase) applications, these nanomaterials can

    help increase the durability and performance of exhaust-

    treatments and reduce harmful emissions in fact, exhaust

    catalysts tend to become poisoned by sulfur and phosphorus that

    are present in conventional lubricant additives. As a matter of fact,

    the stability of the nanomaterials, coupled to the reduction of the

    content of ash-giving metal additives in the lubricant oil formula-

    tion, can lead to an overall reduction of ash emissions and longer

    life of diesel particulate lters.Nanostructured transition metal dichalcogenides, with the

    generic formula MX2 (MW, Mo; XS, Se), whose synthesis

    was rst demonstrated at the Weizmann Institute by Tenne and

    co-workers [79], seem to be very promising materials to be

    dispersed as nanoparticles in the oil matrix. They involve a

    reaction between MO3 and H2S, in reducing atmosphere at high

    temperatures, and the corresponding sulde (WS2 or MoS2) is

    obtained. Many other synthetic routes have also been followed to

    obtain these kinds of nanostructured materials[1012].

    The specic lubrication mechanism ascribed to these metal

    suldes, often called inorganic fullerenes due to their peculiar

    structure of spherical concentric layers, is currently debated; how-

    ever, several studies clearly indicate that an exfoliation process of

    these layers, and the consequent liberation of nanosheets directlyinside the surface contact area, is the prevalent lubricating mechan-

    ism for these systems [13,14]. This is very interesting because the

    lubrication additive is brought directly in the contact area without

    any prior chemical reaction, avoiding the transient period charac-

    teristic of the current additives. It was also hypothesized that these

    nanoparticles behave as nanoball bearings, due to their spherical

    shape, ultra-hardness and nanosize, at least temporarily until they

    gradually deform and start to exfoliate giving rise to the observed

    low friction coefcients investigations involving direct visualiza-

    tion of the nanoparticle behavior in the contact area, over a broad

    pressure range, were attempted by combining Transmission Elec-

    tron Microscope (TEM) and Atomic Force Microscopy (AFM)[15].

    Contents lists available atScienceDirect

    journal homepage: www.elsevier.com/locate/triboint

    Tribology International

    0301-679X/$- see front matter& 2013 Elsevier Ltd. All rights reserved.

    http://dx.doi.org/10.1016/j.triboint.2013.10.018

    n Corresponding author. Tel.:39 011 0904670; fax: 39 011 0904699.

    E-mail address:[email protected] (D. Fino).

    Tribology International 72 (2014) 198207

    http://www.sciencedirect.com/science/journal/0301679Xhttp://www.elsevier.com/locate/tribointhttp://dx.doi.org/10.1016/j.triboint.2013.10.018mailto:[email protected]:[email protected]:[email protected]://dx.doi.org/10.1016/j.triboint.2013.10.018http://dx.doi.org/10.1016/j.triboint.2013.10.018http://dx.doi.org/10.1016/j.triboint.2013.10.018http://dx.doi.org/10.1016/j.triboint.2013.10.018mailto:[email protected]://crossmark.crossref.org/dialog/?doi=10.1016/j.triboint.2013.10.018&domain=pdfhttp://crossmark.crossref.org/dialog/?doi=10.1016/j.triboint.2013.10.018&domain=pdfhttp://crossmark.crossref.org/dialog/?doi=10.1016/j.triboint.2013.10.018&domain=pdfhttp://dx.doi.org/10.1016/j.triboint.2013.10.018http://dx.doi.org/10.1016/j.triboint.2013.10.018http://dx.doi.org/10.1016/j.triboint.2013.10.018http://www.elsevier.com/locate/tribointhttp://www.sciencedirect.com/science/journal/0301679X
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    The present study focuses on MoS2nanoparticles which have to be

    incorporated in engine lubricant oils. A wet synthesis technique has

    been devised within our group[16], which is based on the preparation

    of an aqueous solution of citric acid and ammonium molybdate to

    form a complex of molybdenum(IV) with citric acid, to which a

    suitable amount of ammonium sulde was added to obtain MoS2.

    This technique resorts to a simple and scalable process, and involves

    low cost reagents, instead of other more complex reaction methods.

    An example of the MoS2 particles obtained with this technique isdepicted inFig. 1.Moreover, this synthesis route is extremely versatile

    since it can be adapted for continuous MoS2 particle production, in

    specic devices that allow to control the particle diameter and obtain

    reproducible results in terms of particle size distribution [17,18].

    As previously mentioned, a progressive poisoning of after-

    treatment catalysts occurs due to the presence of species that

    were originally present in the lubricant oil as additives, and which

    are then released into the ue gases after in-cylinder combustion.

    One major requirement for the application of these nanoparticles

    as lubricant oil additives, in substitution to the currently adopted

    ones, is their complete compatibility with the catalytic substrates

    present in the after-treatment line, whose lifetime operation

    should not be affected to any great extent. This analysis is crucial

    for the introduction of such nanosized additives for lubricant oils

    on the market, and in this work was applied to EURO V-compliant

    catalysts for DOC, DPF and SCR systems.

    2. Experimental

    One important requirement for the application of these nano-

    particles as lubricant oil additives is their compatibility with the

    catalytic substrates present in the after-treatment line therefore,

    an assessment was carried out about a possible interaction

    between the MoS2 nanopowders and some commercial catalysts,

    representative of EURO V-compliant catalytic converters present

    in the after-treatment line of light-duty diesel engine vehicles, forwhich a diesel engine bench (OPEL 1900 cm3 JTD common Rail)

    connected to a dynamometer (AVL Alpha 240 kW) with a max-

    imum rpm/torque of 10,000 rpm/600 Nm, was used (schematically

    depicted inFig. 2).

    The experimental campaign was carried out in different steps

    initially, the engine was conditioned with a commercial synthetic oil

    (multi-grade SAE 5W-30 provided by Fuchs Lubricants), through a

    standardized procedure for internal oil circulation before the test was

    started. Then, ve different engine points were tested in order to

    reproduce the different operation conditions of the car (engine

    frequency in rpm and bpme in bar: 15001, 20002, 25003,

    30004 and 35005, all with 0% EGR), and for each engine point

    four different cooling water temperatures of the engine were xed (40,

    60, 80 and 95 1C). The exhaust gas recirculation was xed to zero in all

    operating conditions. These settings were operated through a dedi-

    cated AVL PUMA program, by monitoring all engine conditions with

    INCA software connected to the Electronic Control Unit (ECU) inte-

    grated with ETAS and BOSCH instrumentation the temperature of

    the cooling water, of the engine outlet exhaust gases and of the

    lubricant oil were measured with K-type thermocouples.

    The same procedure was adopted for the MoS2 nanoparticle-

    additivated oil, whose concentration was 0.5 wt%.

    The tests consisted in monitoring and measuring the gas

    composition, particle size distribution, the temperature and pres-

    sure, at each engine point and in each cooling water temperature in

    the engine on steady state. In particular, the gas composition was

    continuously monitored before and after both the Diesel Oxidation

    Catalyst converter (DOC) and the Diesel Particulate Filter (DPF),

    with an ABB gas analyzer, equipped with two Uras26 analyzers for

    N2O, NO, CO2, CO and SO2, and a Magnos206 analyzer to measure

    O2. The HCs were measured with a Multid14 analyzer Hart-

    mann&Braun. The smoke number was measured with a Variable

    Sampling Smoke Meter AVL 415S G002. The soot particle size

    distribution was recorded using a Scanning Mobility Particle Sizer

    3080 (SMPS), which consists of an impactor (type 0.0508 cm), a

    neutralizer, a differential mobility analyzer, and a condensation

    particle counter, with the sheath and aerosol ows set to 6 andFig. 1. TEM micrograph of MoS2nanoparticles.

    Fig. 2. Schematic of the diesel engine bench.

    S.J. Castillo Marcano et al. / Tribology International 72 (2014) 198 207 199

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    0.6 l/min, respectively; this system covered the 9.6422 nm parti-

    cle diameter range, each scan lasted 75 s (scanning time of 60 s

    plus retrace of time 15 s). The engine exhaust was sampled using a

    heated pipe (1 m long, 6 mm diameter,T150 1C), followed by two

    ejector pump diluters in series (Dekati Ltd.) each stage provided a

    dilution factor of8, resulting a 64 fold overall dilution, which was

    calibrated measuring the carbon dioxide concentrations in the

    exhaust and in the sample ow, and then the exiting gas was

    transported to the SMPS system through a 4 m long tube

    (OD6 mm)[19].

    Finally, a long term endurance test was performed, in which the

    oil additivated with MoS2nanoparticles was subjected to 100 h of

    engine operation at 20002 (with a cooling water temperature of

    95 1C and an EGR opening of 22% to accelerate soot accumulation

    in the DPF), corresponding to a total distance of 10,000 km at a

    constant speed of around 100 km/h, with startstop intervals and

    regeneration periods necessary to clean the DPF each time the

    pressure drop across the lter attained 80 mbar, which roughly

    indicated that a 6 g/l soot loading was reached. The regeneration

    was carried at 27507.5. The startstop intervals were important

    to expose the oil to repeated temperature changes, which simulate

    the continuous startstop of the car. Similarly, the regeneration is

    one of the most intensive conditions occurring in engine opera-

    tion, during which the oil containing nanoparticles is exposed to

    several over-injections of diesel in the combustion chamber, to

    reach suitable temperatures in the DPF for soot catalytic oxidation

    [20]. This long term test was meant to see if any ash accumulation

    or catalyst deactivation was observed due to, among others, the

    possible emissions of sulfates ascribable to the MoS2content in the

    engine oil. It has to be pointed out that higher ash loadings have to

    be investigated to be fully representative of the exposure of a DPF

    to ash-containing soot emissions therefore, increased travel

    distances have to be foreseen in the future, such as around

    150,000 km which would correspond to the entire lifetime of a

    DPF, and that the present test is a preliminary assessment of the

    NP-additivated lubricant oil tendency to produce MoS2-related

    ashes (Table 1).

    However, an attempt to quantify the impact of MoS2 in the ash

    composition has been indeed performed the chemical analysis of the

    soot collected in the DPF lter by employing base oil and NP-additivated oil, was performed by an Agilent 7500ce ICP/MS. A sample

    of 100 mg was dissolved in a solution prepared with 3 ml of deionized

    water, 2 ml of hydrogen peroxide and 5 ml of nitric acid (65%

    concentrated). The so-obtained solution was treated in a microwave

    oven (CEM, mod. Mars 250/40) for 1 h, at a maximum temperature of

    180 1C. The mineralized solution was diluted with deionized water to a

    nal volume of 50 ml and subsequently analyzed.

    3. Results and discussion

    Figs. 37 report the particulate emissions measured with the

    SMPS, at ve couples of rpm and bpme (15001, 20002,

    25003, 30004 and 35005), which were tested in order to

    characterize the various operating conditions of the engine. Ineach gure, four water cooling temperatures were tested (40 1C,

    60 1C, 80 1C, and 95 1C), and particulate emissions were sampled at

    the engine outlet (i.e. the DOC inlet), at the DOC outlet (i.e. DPF

    inlet), and at the DPF outlet.

    The comparison between the emissions generated with the

    base oil, and the ones with the additivated one with MoS2nanoparticles, shows the effect of nanolubricant inclusion in the

    oil matrix on the particulate in the exhaust gases. The global

    information based on mass particle concentration are presented in

    Tables 2 and 3, for the base oil and the NP-additivated ones,

    respectively.

    Starting from Fig. 3 at rpm/bpme of 15001, which is a low

    load for the engine, one can notice that the particle size distribu-

    tion at the DOC inlet follows a Gaussian curve, as described by

    Table 1

    Physical properties of the base lubricant oil prior MoS2 additivation.

    Physical property Unit Value

    Viscosity class 5W-30

    Kinetic viscosity (80 1C) mm2 s1 61.5

    Kinetic viscosity (100 1C) mm2 s1 10.1

    Viscosity index 155

    CCS viscosity (30 1C) mPa s 6100

    HTHSV (1501

    C) mPa s 3.1

    Table 2

    Measured soot particle mass concentration (g/m3) before the DOC, before the DPF

    and after the DPF, for the base oil.

    Engine points in DOC in DPF out DPF

    40 1C 15001 6677 2403 0

    20002 18,474 5062 0

    25003 21,205 7936 17

    30004 18,517 7264 1

    35005 20,202 6374 15

    60 1C 15001 15,850 2483 4

    20002 11,221 2246 0

    25003 12,181 5459 6

    30004 19,904 6912 3

    35005 19,882 6496 33

    80 1C 15001 3050 2362 4

    20002 5734 3085 2

    25003 7637 4413 3

    30004 12202 5088 2

    35005 13461 5434 21

    95 1C 15001 6054 3722 22

    20002 9322 3219 9

    25003 7850 4518 13

    30004 11,946 5030 4

    35005 14,698 4976 25

    Table 3

    Measured soot particle mass concentration (g/m3) before the DOC, before the DPF

    and after the DPF, for the NP-additivated oil.

    Engine points in DOC in DPF out DPF

    40 1C 15001 14,122 2387 434

    20002 24,021 5078 1

    25003 19,306 7456 1

    30004 25,813 6816 2

    35005 16,874 7264 4

    60 1C 15001 16,362 3254 584

    20002 11,904 2131 0

    25003 16,277 3296 230004 20,394 4256 1

    35005 16,021 5594 11

    80 1C 15001 10,944 1805 1,750

    20002 32,362 2179 1

    25003 11,370 3270 0

    30004 17,770 4106 2

    35005 14,613 5098 2

    95 1C 15001 7146 1968 1872

    20002 24,928 2342 10

    25003 8800 3027 1

    30004 10,240 4266 18

    35005 12,320 4666 35

    S.J. Castillo Marcano et al. / Tribology International 72 (2014) 198207200

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    Kittelson et al. [21], at all cooling water temperature conditions.

    Similar trends are found in the DOC inlet emissions obtained with

    the base oil and the NP-additivated one, especially at 40 1C, 60 1C

    and 95 1C; however, an evident increase of the ultrane particle

    concentration belonging to the nuclei mode (o50 nm) is observed

    for the oil containing MoS2. The nuclei mode usually includes,

    Fig. 3. Measured soot particle concentration with respect to the particle diameter before the DOC (blue squares), before the DPF (red circles), after the DPF during loading

    (green triangles), for the base oil (open symbols) and the NP-additivated oil (closed symbols). Engine point: 1500 1 and cooling water temperature: (a) 40 1C, (b) 60 1C,

    (c) 80 1C, and (d) 95 1C. (For interpretation of the references to color in this gure legend, the reader is referred to the web version of this article.)

    Fig. 4. Measured soot particle concentration with respect to the particle diameter before the DOC (blue squares), before the DPF (red circles), after the DPF during loading

    (green triangles), for the base oil (open symbols) and the NP-additivated oil (closed symbols). Engine point: 2000 2 and cooling water temperature: (a) 40 1C, (b) 60 1C,

    (c) 801

    C, and (d) 951

    C. (For interpretation of the references to color in this gure legend, the reader is referred to the web version of this article.)

    S.J. Castillo Marcano et al. / Tribology International 72 (2014) 198 207 201

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    besides soot particles, also volatile organic (also called SOF) and

    sulfur compounds that may be formed during exhaust gases'

    dilution and cooling [22]; the latter fraction could represent

    120% of the total mass concentration. The slight increase of the

    nuclei mode for the nanolubricant case is presumably caused by

    the presence of such volatile organic and sulfuric compounds,

    Fig. 5. Measured soot particle concentration with respect to the particle diameter before the DOC (blue squares), before the DPF (red circles), after the DPF during loading

    (green triangles), for the base oil (open symbols) and the NP-additivated oil (closed symbols). Engine point: 2500 3 and cooling water temperature: (a) 40 1C, (b) 60 1C,

    (c) 80 1C, and (d) 95 1C. (For interpretation of the references to color in this gure legend, the reader is referred to the web version of this article.)

    Fig. 6. Measured soot particle concentration with respect to the particle diameter before the DOC (blue squares), before the DPF (red circles), after the DPF during loading

    (green triangles), for the base oil (open symbols) and the NP-additivated oil (closed symbols). Engine point: 3000 4 and cooling water temperature: (a) 40 1C, (b) 60 1C, (c)

    801

    C, and (d) 951

    C. (For interpretation of the references to color in this gure legend, the reader is referred to the web version of this article.)

    S.J. Castillo Marcano et al. / Tribology International 72 (2014) 198207202

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    which are precursors of the nucleation of the soot particles. The

    effect of NP-additivation is also evident in terms of total mass

    concentration (Tables 2and3), where the engine out emissions are

    greater with respect to the base oil, at all investigated cooling

    temperatures.

    If one focuses on the DOC outlet (i.e. DPF inlet) emissions ofFig. 3,

    a signicant change in the particle size distribution can be noticed

    across the DOC itself, for all tested temperatures the nuclei mode is

    mostly affected (o50 nm), while the accumulation mode (450 nm)remains quite constant due to the fact that the carbonaceous soot,

    which belongs to the latter class[21], is refractory to oxidation at the

    normal DOC operating temperatures. As far as the oil is concerned,

    the particulate emissions with the base oil exhibit almost the same

    prole at all investigated temperatures, this being quite similar to the

    ones with the NP-additivated oil at 40 1C and 60 1C. Whereas, they

    strongly differ at higher temperatures (80 1C and 95 1C), where the

    emissions observed with the nanolubricant are surprisingly lower

    than the ones with the base oil. This is also testied by the

    comparison of the emissions in terms of mass concentration

    (Tables 2 and3). A possible explanation will be later attempted in

    relationship to gaseous emissions.

    Finally, the particle size distribution at the DPF outlet in Fig. 3

    shows a signicant difference between the two lubricant oils a

    much higher concentration of the particles are noticed in the

    nanolubricant case for all investigated temperatures, although this

    concentration is reduced by two orders of magnitude with respect

    to the engine outlet. This behavior occurs only for this particular

    rpm/bmep couple, while for all other conditions the base and

    NP-additivated oils behave in the same way in terms of outlet DPF

    emissions (Figs. 47); it could be caused by the low exhaust

    gas temperatures at this engine point, and in particular in the

    coolest part of the after-treatment line (no DPF regeneration was

    performed during sampling), which may be below the dew point

    of some heavy hydrocarbons that undergo nuclei condensation.

    In the case at 20002 (Fig. 4), the engine out emissions

    overlap for the two oils, except for the part of the curve at low

    particle diameters, whose concentration is higher for the nanolu-

    bricant than for the blank. However, as for the above-mentioned

    lower engine load, the DOC atters these proles, and demon-

    strates to be more efcient in oxidizing the nest part of the curve

    obtained with the nanolubricant, rather than with the base oil.

    Again, this can be globally observed in terms of mass concentra-

    tion in Tables 2 and 3. The DPF is almost 100% efcient in sootabatement, irrespective of the tested oil matrix.

    At increasing load, it can be observed that the differences

    between the base oil and the NP-additivated oil still remain, but

    tend to decrease (Figs. 57). The greater engine outlet emissions

    of soot ascribable to the original MoS2 presence in the lubricant

    oil are limited to the nest particles, while in terms of total mass

    their concentration equals the one obtained with the base oil in

    most of the experiments (Tables 2and3). An indirect information

    of this behavior is testied by the similar smoke numbers

    recorded at the engine outlet (Fig. 8a) for the two oils. The

    problem of ultrane particle generation has almost no impact

    downstream of the DPF.

    The effect of sulfur in MoS2is also quite limited in terms of SO2emissions, the latter being around 34 ppm, while the ones

    measured with the base oil are below the detection limit

    (Fig. 8b) in fact, less than 10 ppm of S is present in the fuel,

    therefore the dilution factor introduced by air brings the concen-

    tration of SO2 in the exhausts below 1 ppm. As a result, the

    poisoning effect of sulfur originated from MoS2 should therefore

    be very low, and not relevant throughout the catalysts lifetime,

    due to very low SO2 concentration in the exhausts.

    Further information of the effect of MoS2 additivation to a

    lubricant oil comes from the analysis of the gaseous emissions of

    HC, CO and NO at the engine outlet (i.e. DOC inlet, Fig. 9), DOC

    outlet (i.e. DPF inlet, Fig. 10) and DPF outlet (Fig. 11).

    Fig. 7. Measured soot particle concentration with respect to the particle diameter before the DOC (blue squares), before the DPF (red circles), after the DPF during loading

    (green triangles), for the base oil (open symbols) and the NP-additivated oil (closed symbols). Engine point: 3500 5 and cooling water temperature: (a) 40 1C, (b) 60 1C, (c)

    801

    C, and (d) 951

    C. (For interpretation of the references to color in this gure legend, the reader is referred to the web version of this article.)

    S.J. Castillo Marcano et al. / Tribology International 72 (2014) 198 207 203

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    Starting from HC and CO engine outlet emissions (Fig. 9), it can be

    observed that their amounts are greater at both low engine points

    (due to their low efciency) and high ones (due to the higher fuel

    consumption, and therefore higher emissions), while they are lower

    at intermediate ones (due to a better compromise of efciency and

    reduced slip of species from incomplete fuel combustion). Moreover,

    increasing water temperatures tend to reduce the emissions of

    partially oxidized species like CO. It can be seen that the emissions

    of HC and CO emitted by the engine are higher in the presence of the

    nanolubricant than in its absence, regardless of the engine point.

    This has a strong relationship between HC and soot emissions

    hydrocarbons are precursors of soot particle nucleation, and their

    concentration in the exhaust gases could inuence the particle sizedistribution and mass concentration, thus being responsible for

    the higher soot emissions observed with the NP-additivated oil. In

    addition, higher HC concentrations involve that greater amounts

    of heavy hydrocarbons fractions adsorb inside the porous struc-

    ture of the particle and on its surface, thus conferring a higher

    reactivity towards oxidation with respect to the sole carbonaceous

    structure of soot, which is much refractory.

    Fig.10 shows that the DOC tends to reduce the differences between

    the emissions measured with two oils the higher temperatures of

    the exhaust ue gases at high loads cause a consistent reduction of the

    CO and HC emissions, while the ones of NO remain almost unchanged.

    The same happens at the DPF outlet (Fig. 11), and the slight increase of

    CO is ascribed to the DPF passive regeneration, although almost

    negligible in terms of soot combustion rate.

    It can be concluded that, although the emissions of soot

    particles are higher in the presence of MoS2 in the lubricant oil,

    especially in terms of ultrane particles, the DOC is able to reduce

    the mass and number concentration of these particles down to

    levels comparable (or even lower) than in the case of base oil. This

    is possible because of the higher hydrocarbon concentration in the

    gas, and consequently, absorbed in the solid particulates, which

    confers a greater reactivity to the soot particle itself. Moreover, the

    DPF emissions are absolutely similar for both oil matrixes, with the

    exception of the engine point at 1500 1 for the above-discussed

    reasons. In this regard, it can be stated that the MoS2 as

    nanolubricant does not entail neither higher tailpipe emissions,

    Fig. 8. Measured smoke number and SO2concentration before the DOC at different

    engine points for the NP-additivated oil (red) at various cooling water temperatures

    (40 1C, 60 1C, 80 1C and 95 1C, from dark to light) and SO2concentration for the base

    oil below the detection limit. (For interpretation of the references to color in this

    gure legend, the reader is referred to the web version of this article.)

    Fig. 9. Measured CO, HC and NO concentration before the DOC at different engine

    points for the base oil (blue) and the NP-additivated oil (red) at various cooling

    water temperatures (40 1C, 60 1C, 80 1C and 951C, from dark to light). (For

    interpretation of the references to color in this gure legend, the reader is referredto the web version of this article.)

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    nor any incompatibility with the after-treatment line. In addition,

    the after-treatment catalysts are able to reduce the HC and CO

    emissions down to levels quite similar for the base and

    NP-additivated oil, which indicates a full compatibility of the

    investigated catalysts towards the MoS2nanolubricant.

    A challenge which remains undisclosed in the former tests is

    the long-term performance of the catalysts for this reason, an

    endurance test was tailored to monitor the catalyst efciency

    throughout a 100 h-lasting test, with intermediate DPF regenera-

    tions. The engine point at 20002 was selected (at a cooling water

    temperature of 95 1C and an EGR opening of 22%) for the soot

    loading phase. The regeneration was carried out when 80 mbar

    was attained at 20002, which corresponds to 215245 mbar at

    27507.5, depending on the temperature of the exhaust gases

    during the regeneration itself.

    Fig. 12 reports the four regenerations (each one lasting 5 min

    from the time of attainment of 580 1C at the DPF inlet) that were

    performed throughout the tests in terms of DPF pressure drop and

    of inlet and outlet DPF temperatures, while the loading is not

    depicted for the clarity of the gure. It can be seen that, at

    increasing inlet DPF temperature, the pressure drop increases due

    to the higher gas viscosity; however, at appropriate temperatures

    for soot ignition, the regeneration starts and the soot consumption

    Fig. 10. Measured CO, HC and NO concentration before the DPF at different engine

    points for the base oil (blue) and the NP-additivated oil (red) at various cooling

    water temperatures (40 1C, 60 1 C, 801C and 95 1C, from dark to light).

    (For interpretation of the references to color in this gure legend, the reader isreferred to the web version of this article.)

    Fig. 11. Measured CO, HC and NO concentration after the DPF at different engine

    points for the base oil (blue) and the NP-additivated oil (red) at various cooling

    water temperatures (40 1C, 60 1C, 80 1C and 951C from dark to light). (For

    interpretation of the references to color in this gure legend, the reader is referredto the web version of this article.)

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    is evident in terms of pressure drop decrease and outlet DPFtemperature increase above the inlet one [23]. Anyhow, the most

    important outcome of these four repeated regenerations is that a

    full recovery of the original pressure drop (50 mbar at 27507.5)

    was attained. This indicates that the same degree of soot removal is

    obtained in repeated regeneration cycles, without any noticeable

    ash accumulation. Hence, its occurrence would progressively

    decrease the clean lter permeability and reduce the ltration area

    available for soot cake build-up[24].

    Moreover, the ash content in the soot emitted by the engine

    was quantied to further assess the potential of ash accumulation

    in the DPF. This has been carried out by collecting samples of soot

    in the DPF, when both the base oil and the NP-additivated oil were

    employed. The soot samples were analyzed by means of ICP-mass,

    and the results are reported inTable 4. Elements under or close to

    the detection limit (0.001 wt%) are not reported. The total amount

    of ashes was measured to be 10.1 and 7.5 wt% when the base oil

    and the NP-additivated oil were respectively employed. This

    demonstrates that the MoS2 nanolubricant is able to reduce the

    content of ashes in soot, whose explanation was attempted

    through the following analysis of the metal elements in the ashes.

    The elements are divided into wear metals, meaning ele-

    ments coming from the abrasion of engine components, mainly

    constituted by steel, aluminum alloys as well as cast iron, and

    additive metals, meaning elements deriving from compounds

    employed as additives in the oil. As can be noticed, the tendency

    for wear metals is their general slight decrease when using the oil

    additivated with MoS2nanoparticles. This is probably ascribed to a

    reduced abrasion of the engine parts, and consequently a decrease

    of the friction coefcient.

    The same trend can be depicted for the elements coming from

    additives, except for sodium and zinc, due to a different additive

    formulation for the oil containing MoS2 nanoparticles in fact,

    their benecial presence allows to have a reduced content of anti-wear additives.

    Concerning molybdenum, the quantity measured in the two

    soot samples is the same, meaning that the presence of MoS2nanoparticles in the additivated oil does not in any way affect the

    nal content of Mo in the soot.

    Finally, no clear deactivation of the soot oxidation catalysts

    occurs due to the specic soot emissions obtained with the NP-

    additivated oil, or due to the presence of MoS2-related SO2 in the

    exhaust gases, due to the same degree of regeneration completion

    after 5 min in all regeneration runs.Table 5reports the emissions

    before the four regenerations occurred during the 100 h of tests at

    20002 with 22% EGR, as well as at the beginning and at the end

    of the test at 20002 with 0% EGR (the latter being the same

    condition depicted inFig. 4d for the soot emissions, andFig. 9for

    Fig. 12. Measured inlet and outlet DPF temperatures (black and red curves, respectively, referred to the left y-axis) and pressure drop (gray dots, right y-axis) during

    successivelter regenerations (from a to d) during the long-term endurance test of 10 h. For the related gaseous emissions, seeTable 5. (For interpretation of the references

    to color in this gure legend, the reader is referred to the web version of this article.)

    Table 4

    Results of the chemical analysis by ICP-mass on the soot collected in DPF by using

    base oil and NP-additivated oil.

    Element [wt%] Base oil NP-additivated oil

    Wear metals Aluminum 0.169 0.115

    Copper 0.235 0.243

    Iron 0.499 0.477

    Manganese 0.122 0.121

    Nickel 0.033 0.027

    Molybdenum 0.757 0.740

    Additives Boron 0.036 0.016

    Calcium 7.081 5.012

    Magnesium 0.251 0.088

    Phosphorus 0.519 0.373

    Potassium 0.078 0.038

    Sodium 0.059 0.083

    Zinc 0.098 0.110

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    the gaseous ones). It can be seen that no substantial differences in

    HC, CO and NO concentration at the engine outlet occur through-

    out the entire test, which ensures that no specic degradation

    affects the MoS2-containing oil after a test corresponding to a

    traveled distance of 10,000 km.

    Longer endurance tests might disclose further information on

    this matter, but 100 h still indicates that the interaction between

    the emissions from an engine lubricated with MoS2-formulated

    oils and state-of-the-art EURO V catalysts, does not involve any

    long-term decrement in emission abatement..

    4. Conclusions

    A novel wet chemical synthesis method has been developed for

    the production of molybdenum(IV) sulde nanopowders, which

    are used as lubricant additives (0.5 wt%) in this work.

    The MoS2-additivated lubricant oil was tested in a real diesel

    engine in fact, in the perspective of a practical application on-

    board the vehicle, one has to carefully address the issues of

    pollutant emissions possibly related to the new oil, and the

    emission abatement efciency of the catalytic converters.

    Irrespective of the investigated engine point, the emissionsrecorded by the SMPS showed an increase of ultrane particles

    associated to the use of the NP-additivated oil, which presumably

    mainly constituted SOF which form an aerosol, and are absorbed

    on soot particles or form individual nuclei. This consideration

    derives from the remarkable abatement efciency of the DOC

    towards these particles, both in terms of number and mass

    concentration, which lowers their emissions down to the same

    levels encountered in the tests with the reference base oil, or even

    below. A similar increase of HC and CO emissions is also recorded

    in the gas phase at the engine outlet, which again suggests that the

    presence of nanoparticles in the lubricant might induce some little

    but not negligible modications of the combustion regime. SO2showed a 4 ppm emission in the exhausts, which reasonably

    excludes any major poisoning effects of the after-treatmentcatalysts.

    In order to check the long-term compatibility of the above-

    mentioned DOC and DPF when exposed to the ue gases produced

    when the NP-additivated oil was used, a 100 h test was performed.

    The engine gaseous emissions were stable throughout the whole

    test. The possibility of an anomalous ash production and progres-

    sive accumulation inside the diesel particulate lter was excluded

    the retention in the lter of the soot incombustible fraction,

    originated from current fuel and lubricant additives, did not cause

    any progressive reduction of the available ltration area, which

    would have increased the bare lter pressure drop at the end of

    each repeated regeneration. It is worth mentioning that longer

    accumulation tests should be performed to comprehensively

    assess the ashing tendency of the NP-additivated oil.

    As a result of the present work, the possible advantage arising

    from the nanoparticle embodiment in the lubricating oil, which is

    meant to provide friction and wear reduction, was demonstrated

    not to be offset by any possibly MoS2-related reduced abatement

    efciency or stability loss of the after-treatment catalysts.

    Acknowledgments

    The ADDNANO Project, funded by the European Commission as

    part of the 7th Framework Programme, is gratefully acknowledged

    for the nancial support.

    Dr. F. Stanzione is gratefully acknowledged for the contribution

    related to ICP/MS analyses.

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    Table 5

    Measured CO, HC, NO, SO2 and CO2concentration at the engine outlet for the NP-

    additivated oil during the long-term test, carried out at 20002 with a water

    temperature of 95 1C and 22% of EGR, and compared to the ones at 0% of EGR.

    EGR (%) Time (h) CO (ppm) HC (ppm) NO (ppm) SO2(ppm) CO2 (%)

    0 0 218 76 140 3 2.62

    100 187 76 141 3 2.4922 0 517 30 38 5 4.86

    23 455 23 31 5 4.3248 452 20 33 5 4.49

    74 440 19 34 5 4.55

    100 511 23 33 6 4.80

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