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A study was conducted to assess the effects of a water-diesel fuel emulsion with and without an oxidation catalytic converter (OCC) on steady-state heavy-duty diesel engine emissions. Two OCCs with different metal loading levels were used in this study. A 1988 Cummins L10-300 heavy-duty diesel engine was operated at the rated speed of 1900 rpm and at 75% and 25% load conditions (EPA modes 9 and 11 respectively) of the 13 mode steady-state test as well as at idle. Raw exhaust emissions' measurements included total hydrocarbons (HC), oxides of nitrogen (NOx) and nitric oxide (NO). Diluted exhaust measurements included total particulate matter (TPM) and its primary constituents, the soluble organic (SOF), sulfate (SO42-) and the carbonaceous solids (SOL) fractions. Vapor phase organic compounds (XOC) were also analyzed. The SOF and XOC samples were analyzed for selected polynuclear aromatic hydrocarbons (PAHs).

Exhaust emissions of non-methane hydrocarbon (NMHC) and methane were measured from a Tier 3 dual-fuel demonstration locomotive running diesel-natural gas blend. Measurements were performed with the typical flame ionization detector (FID) method in accordance with EPA CFR Title 40 Part 1065 and with an alternative Fourier-Transform Infrared (FTIR) Spectroscopy method. Measurements were performed with and without oxidation catalyst exhaust aftertreatment. FTIR may have potential for improved accuracy over the FID when NMHC is dominated by light hydrocarbons. In the dual fuel tests, the FTIR measurement was 1-4% higher than the FID measurement of. NMHC results between the two methods differed considerably, in some cases reporting concentrations as much as four times those of the FID. However, in comparing these data it is important to note that the FTIR method has several advantages over the FID method, so the differences do not necessarily represent error in the FTIR.

A heavy-duty 320 kW diesel engine has been converted to natural gas operation. Conversion technology was selected to minimize costs while reaching NOx emissions goals of less than 3.2 g/kW-hr. Two engines are being converted using quiescent and high swirl combustion systems. The first engine with low swirl cylinder heads of the base diesel engine, and a combustion system developed for it was tested on a steady state cycle that has been shown to simulate the US heavy duty transient test cycle. It shows NOx emissions of 2.9 g/kW-hr and total HC emissions of 5.4 g/kW-hr. It is suspected that the HC emission is high because of high valve overlap. Experience with other similar engines suggests that non-methane HC emission is about 0.4-0.8 g/kW-hr. It is also expected that modified valve events and/or an oxidation catalyst can reduce HC emissions to much lower levels. The efficiency of the low swirl natural gas engine at this NOx level is 36 percent at rated condition.

Development of methodology for diesel hydrocarbon speciation of C12-C22 compounds and the application of that methodology to determine total ozone forming potential of diesel exhaust emissions is an extremely complicated task. Methodology has already been developed for speciating C1-C12 exhaust emissions from engines and vehicles fueled with gasoline, diesel, and alternate fuels. However, very little or no information is available for exhaust speciation of C12-C22 compounds as sampling and analytical constraints make the collection and analysis of the higher molecular weight compounds extremely challenging. Key issues related to the definition of “hydrocarbons” also need to be addressed prior to promulgation of future reactivity-based legislation for diesels (e.g., Which exhaust hydrocarbon compounds actually exist in gas-phase and participate in atmospheric ozone formation?).

Regulated gaseous, particulate and several unregulated emissions are reported from four heavy-duty diesel engines operated on the chassis version of the 1983 transient procedure. Emissions were obtained from Caterpillar 3208, Mack ENDT 676, Cummins Formula 290 and Detroit Diesel 8V-71 engines with several diesel fuels. A large dilution tunnel (57′ × 46″ ID) was fabricated to allow total exhaust dilution, rather than the double dilution employed in the stationary engine version of the transient procedure. A modal particulate sampler was developed to obtain particulate data from the individual segments of the 1983 transient procedure. The exhaust gas was analyzed for benzo(a)pyrene, metals, N2O, NO2, individual hydrocarbons and HCN. Sequential extractions were performed and measured versus calculated fuel consumptions were obtained.