Abstract
This study examines the composition and combustion performance of biodiesel produced from waste cooking oil. Six fuel batches produced from waste oil used in dining-hall fryers were examined to determine their physical and chemical properties, including their elemental and fatty acid methyl ester composition. Oleic and linoleic methyl esters accounted for more than 70% of the fuel composition, while the oxygen content averaged 10.2% by weight. Exhaust emissions were monitored for 5–100% biodiesel blends using two off-road engines: a 2007 Yanmar diesel generator and a 1993 John Deere front mower. Increasing biodiesel content resulted in reduced emissions of partial combustion products from the diesel generator but a rise in NOx, with the greatest changes occurring between 5 and 20% biodiesel content. For the riding mower, biodiesel content up to 50% had little effect on emissions, while NOx and total hydrocarbon emissions decreased with 100% biodiesel. The difference in NOx emissions is attributed to the two different fuel injection control designs used in the two engines. These results indicate that the effects of biodiesel use on nonroad engine exhaust emissions may be substantially lower in older engines optimized for performance over emissions control.
1. Introduction
Rising fuel costs and energy demands, combined with growing concern over greenhouse gas emissions, have led to increased interest in the use of renewable fuels to help meet increasing worldwide fuel demand and reduce atmospheric CO2 emissions from transportation sources [1–3]. Biodiesel is an oxygenated diesel fuel composed primarily of fatty acid methyl esters that can be produced from a variety of vegetable oils and animal fats [4]. It can be used directly in existing diesel engines, either as a fuel replacement or as an additive to improve combustion processes [5]. In addition, biodiesel fuels may help to reduce emissions of some toxic air pollutants [6, 7].
Biodiesel can be produced from a range of vegetable oils and animal fats. The use of soybean oil and other high-quality food-grade vegetable oils presents economic difficulties because of competition with use for food products. One more economically feasible source for biodiesel is waste cooking or frying oils, also known as yellow grease. As a waste product, used cooking oil is a potentially cheaper feedstock than edible vegetable oils [8], and does not directly compete with the growth of food crops. Estimates for potential biodiesel production from waste cooking oil in the United States range from 100 to 200 million gallons per year, although recent production levels from these sources are only around a tenth of this amount [9, 10]. As with most other vegetable-oil-based fuels, waste cooking oil (WCO) biodiesel has a higher viscosity, cetane number, and density than conventional diesel [11], but it can meet existing fuel property standards [12].
The composition of WCO biodiesel varies somewhat depending on the oil feedstock and the fuel production process. Most vegetable oil feedstocks consist primarily of C16 and C18 fatty acids, but can also include smaller contributions from other C8 to C22 compounds [13]. In addition to differences in cooking oil stocks, variations in frying temperatures and times can affect the composition of the final fuel. Several studies have identified oleic and linoleic acid as the predominant fatty acid methyl esters present in WCO biodiesel [14, 15]. In a study of used cooking oils, however, Knothe and Steidley [16] observed high variability in WCO fatty acid composition from different restaurants and between batches at the same location, which could result in similar variability in the biodiesel.
Several comprehensive reviews of the existing literature have concluded that biodiesel use will generally reduce exhaust emissions of particulate matter, total hydrocarbons, and carbon monoxide [6, 7]. Published experiments using WCO biodiesel are generally in line with these trends [17–20]. Di et al. [21] observed a decrease in total hydrocarbon (THC) emissions in blends of WCO biodiesel with ultralow sulfur diesel (ULSD), with the greatest reductions (50%) achieved with pure biodiesel. However, Lin et al. [22] found that a 20% blend of waste cooking oil biodiesel and conventional diesel produced lower carbon monoxide (CO) emissions than either pure fuel.
The effects of WCO biodiesel on emissions of nitrogen oxides () are less predictable. Several studies have reported reductions in total emissions for pure WCO biodiesel compared to number 2 diesel [17, 19], while others have reported increases [18] or no substantial effect [23]. Di et al. [21] and Lin et al. [22] observed increases in emissions when WCO biodiesel fuels were blended with ultralow sulfur diesel and premium diesel, respectively. Dorado et al. [20] observed different results based on speciation, with nitric oxide (NO) concentrations decreasing by 37% but nitrogen dioxide (NO2) concentration increasing by up to 81%. Some of this variation between studies may be due to the greater sensitivity of emissions to engine combustion conditions [24]. Additionally, differences in the chemical properties and cetane number of WCO biodiesel compared to petroleum diesel fuel will influence injection timing and subsequent premixed and diffusion burn characteristics during combustion, all of which can affect production [25–28].
In the mid 1990s, U. S. EPA began implementing emissions standards for off-road diesel engines that established maximum permitted levels for CO, , and hydrocarbon emissions [29]. These standards were phased in using a series of progressively stricter emissions requirements, or tiers. Initial application of Tier 1 standards occurred from 1996–2000 (depending on engine size), with Tier 2 and Tier 3 regulations going into effect from 2001–2006 and 2006–2008, respectively. As these regulations apply only to newly built engines, older agricultural and construction equipment built before 1996 are not subject to these controls. In addition, stationary diesel engines were not covered by these regulations until 2007. As off-road equipment may have a lifespan of several decades or more, diesel engines currently in use are subject to a wide range of emissions regulations, ranging from no controls for older engines to strict Tier 4 standards for the newest equipment.
One particular area of concern for off-road equipment is emissions produced during idling. Since idling engine speed is relatively low, and only a small amount of fuel is added in order to maintain engine crankshaft revolution, combustion efficiency drops significantly. This results in higher hydrocarbon emissions and partial combustion products that are hazardous to the environment and the health of the user [30]. In developing representative test cycles for off-road engines, Graham et al. assigned a weighting factor of 15% to account for idling in a weed trimmer activity profile [31]. The ISO 8-Mode Cycle for steady state testing of engines weighs idle similarly at 15% [32].
The current study examines biodiesel produced from waste cooking oil feedstocks at the University of Kansas using a small-scale batch reaction process. Multiple batches of WCO biodiesel were analyzed to determine batch-to-batch variation in physical and chemical properties. One batch of the WCO biodiesel was then blended with number 2 diesel to create fuels with 5–100% biodiesel by volume. These fuels were used to power two nonroad engines under idling conditions. Exhaust emissions were analyzed to determine concentrations of CO2, CO, (NO + NO2), and THC. The results are used to evaluate the suitability of WCO biodiesel blends for related off-road applications and to assess the relative importance of fuel makeup and engine operations on pollutant emissions.
2. Experimental
2.1. Fuel
Biodiesel used in this study was produced by the University of Kansas Biodiesel Initiative, utilizing used cooking oil obtained from the University of Kansas dining halls and local restaurants. This used oil was processed to biodiesel in an on-campus pilot scale facility by conversion of the triglyceride fats to fatty acid methyl esters via base-catalyzed transesterification. Each batch of fuel produced was tested for compliance with ASTM standards for density, viscosity, and flash point. Samples from six biodiesel batches produced in 2009 and 2010 were analyzed to determine their hydrocarbon composition. For the emissions experiments, one batch of WCO biodiesel was blended with number 2 petroleum diesel fuel purchased commercially by the KU Maintenance and Operations Department. The fuels were mixed by hand to create five gallons each of 5%, 25%, 50%, and 75% by volume biodiesel blends (identified in this paper as B5, B20, B50 and B75 fuels, resp.). The blended fuels were used in the engine tests within ten days after mixing.
2.2. Fuel Composition Analysis
An Agilent 6890 gas chromatograph coupled with an Agilent 5973N mass spectrometer (GC-MS) was used for fatty acid methyl ester (FAME) analysis of the WCO biodiesel fuels. The chromatographic column was an HP-INNOWax Polyethylene Glycol column of 15 m length mm i.d. 0.5 μm film thickness. Data collection and analysis were performed with HP Chemstation software. A certified standard containing C8–C24 FAMEs was supplied by SUPELCO. Ethyl stearate, supplied by Sigma, was used as an internal standard.
Fuels were prepared for analysis by adding 0.1 mL biodiesel samples to 100 mL of n-hexane. One microliter of this mixture was injected into the GC-MS, which was programmed at 120°C for 1 min, then ramped at 6°C/min to 180°C, 1.5°C/min to 198°C, 5°C/min to 228°C, and then held at 228°C for five minutes. The total run time was 34 minutes. The injection port and transfer line were held at 250°C. Samples were injected in splitless mode with helium as the carrier gas with a flow through the column of 1.4 mL/min. The mass spectrometer used electron ionization at 70 eV, with an ion source temperature of 230°C and quadrupole temperature of 150°C. The electron multiplier was operated at 1482 V, and the solvent delay was 2.5 min.
Individual fatty acid methyl esters present in each biodiesel sample were identified based on GC retention time compared to the known FAME standard compounds and mass spectrum analysis. The response factors of each compound relative to the internal standard were then used to quantify the mass present. The mass detection limit was ng, as determined by analysis of diluted FAME standard solutions. Relative standard deviations (RSDs) for each fatty acid methyl ester were less than 6%, giving an error of 0.6% for a component comprising 10% of the total mass. For each fuel sample, the results of this compositional analysis were used to estimate the fuel H : C ratio and oxygen content. Samples of four of the six fuels were also sent to a commercial testing laboratory for determination of elemental carbon, hydrogen, and oxygen content using ASTM D5291 and ASTM 5622.
2.3. Test Engines
Two engines were used in these experiments: a Yanmar Model 3TN75RJ installed in a 1993 F1145 John Deere Front Mower, and a Yanmar L100V6 installed in a 2007 YDG 5500EV diesel generator. Specifications for both engines are listed in Table 1. The generator engine uses direct injection with a mechanical fuel pump-line injector at a pressure of 19.6 MPa. The front mower engine is also direct injection, with a mechanical unit injector at the same injection pressure. The majority of the experiments were performed on the generator engine, which was purchased new and had less than 50 hours run time prior to the beginning of these experiments. The mower, which had been in service by the University of Kansas Grounds and Maintenance Division since its initial purchase in 1993, was used to provide comparative emissions data from an older engine.
2.4. Emissions Test Procedure
The Yanmar generator was located in a test cell under controlled atmospheric conditions, with an ambient temperature between 23.0 and 24.5°C during all tests. Five different biodiesel blends (Petroleum Diesel, B5, B20, B50, and B100) were tested in a rotating order each day for six days, ensuring that each fuel was in each position once. During the final two experiments, a sixth blend, B75, was also tested. Between each test, the gas tank was completely drained and rinsed several times with the fuel for the next test. During each test, the engine was fully warmed up for 30 minutes prior to the beginning of data collection. Emissions were then monitored for 30 minutes. All experiments were performed with the generator at zero added loading.
Biodiesel combustion experiments with the mower were performed outdoors at the University of Kansas. Ambient temperatures during the test period varied from 13.5°C to 28.0°C. The variation within a given day was between 3 and 4°C, while the largest mean temperature difference between the six test days was 10°C. Four different biodiesel blends, were used in these tests: B5, B20, B50, and B100. Since the mower had been operating on a B5 mixture for more than a year before the beginning of the experiment, no tests were performed with 100% petroleum diesel. Daily testing followed the same procedure as described above for the generator tests, except that not all fuels were tested on each day. The engine was set to idle throughout each experiment.
2.5. Emissions Collection and Analysis
The exhaust pipe from each engine was attached to a high-speed exhaust flow meter (EFM-HS; Sensors, Inc.) using one foot (0.30 m) of metal tubing attached to seven feet (2.1 m) of silicon hose connectors. Heated exhaust was pulled from the flow meter at a rate of eight L/min and transferred by heated line to the emission analyzer. The heated line maintained the exhaust at 192°C to prevent water and total hydrocarbon condensation. Ambient temperature, absolute humidity, and exhaust gas temperature were continuously monitored and recorded via an external weather probe throughout each experiment.
Analysis of gas-phase exhaust constituents was carried out using a SEMTECH-DS portable emissions analyzer (Sensors, Inc.). This instrument measures CO2 and CO concentrations by using nondispersive infrared spectroscopy (NDIR), NO and NO2 by nondispersive ultraviolet spectroscopy (NDUV), and THC using a heated flame ionization detector (FID). An auxiliary electrochemical sensor provided simultaneous O2 measurements. The analyzers were calibrated at the beginning and end of each day using ambient air as the reference zero condition.
Raw concentrations were converted to fuel-specific mass emissions using the SEMTECH analytical software. This is accomplished by composing an overall carbon balance in the exhaust to estimate the total amount of fuel consumed. The calculation for the fuel-specific emissions is shown below for NO [33]: where NOfs is the fuel-specific NO concentration (g/g fuel), is the measured CO2 concentration minus the ambient CO2 concentration determined during calibration, MWNO and MWfuel are the “molecular weights” of NO and the fuel, respectively, and all concentrations are in parts per million (ppm). MWfuel is not a true average molecular weight of the fuel, but a value based on the formula , where is the number of hydrogen atoms per atom carbon in the fuel. For the biodiesel blends used, an adjusted MWfuel formula of , where is the number of oxygen atoms per carbon atom, was used to account for the oxygen content of the fuels.
2.6. Statistical Analysis
An analysis of variance (ANOVA) test was performed to estimate the effects of biodiesel content and other factors on the fuel-specific emissions. The investigators used a general linear model, with biodiesel percentage and the test order of the different blends as the fixed effects. Ambient temperature, exhaust temperature (measured at the exhaust flow meter and used as a surrogate for engine temperature during combustion), and absolute humidity were chosen as covariates. A Pearson correlation analysis was performed on the influence factors that were reported to be statistically significant for two or more pollutants for each engine to test for the linearity and direction of the correlation. All statistical analyses were performed using MiniTab and all variables were tested at the 95% confidence interval.
3. Results and Discussion
3.1. Biodiesel Composition and Properties
The waste cooking oil biodiesel consisted primarily of C16 to C20 esters, with oleic and linoleic acids accounting for at least 75% of the total mass of each sample (Table 2). The two samples analyzed in 2009 had higher concentrations of more saturated compounds, particularly palmitic acid, and an overall composition similar to used frying oils characterized by Mittelbach and Gangl [15]. The four samples from 2010 had higher concentrations of less saturated C18 FAMEs and a greater proportion of longer chain compounds. These differences could be due either to differences in cooking time and temperature, which can increase the saturated FAME content [16], or to variations in the cooking oil feedstocks. Both peanut and canola oils are used at the locations providing the waste cooking oil for this study, with peanut oil having a higher palmitic oil content [34]. The remaining fraction, including uncharacterizable materials, was less than 6% of the total carbon for all samples. There was very little variation in the density of the six fuels, with values ranging from 873–886 g/L and an average of g/L (an RSD of 0.5%). The kinematic viscosity showed slightly more variation, ranging from 4.55–5.03 mm2/s, with an average of mm2/s (RSD of 4.8%). There was no apparent correlation between fuel composition and variations in either the density or viscosity.
For the 2010 fuel samples, the bulk fuel composition results obtained from GC-MS analysis were verified by estimating the calculated H : C ratio and fuel oxygen content based on the FAME composition of the fuel and comparing these predicted values to actual values determined by direct elemental analysis (Table 3). The estimated and total oxygen compositions are in close agreement for WCO4 and WCO5, while the WCO3 and WCO6 estimated values are slightly lower than the measured results due to the higher content of unquantifiable material in those two samples. Actual H : C ratios were similar to predicted values with the exception of WCO3, which had a measured H : C ratio significantly below the value estimated from FAME analysis. This fuel also had the highest viscosity of all six fuels, suggesting either a less-complete transesterification reaction or the presence of non-reactable contaminant materials in the waste cooking oil used for this batch.
A single batch of the waste cooking oil biodiesel (WCO1) was used in all of the emissions experiments, in order to minimize any effects due to fuel quality variations. Table 4 lists specific properties of this fuel, as well as of the B5–B75 blends created through mixing with petroleum diesel. The H : C ratio and oxygen content for the B100 fuel were calculated from the FAME profile for the WCO1 fuel. The H : C ratio for each blend was estimated from a linear combination of the B100 fuel and the number 2 diesel. Similarly, the oxygen content was calculated as a mixture of the two end-member fuels, with the number 2 diesel assumed to have 0% oxygen. Other properties were measured individually for each fuel blend. All measured properties met ASTM D6751 specifications. The measured viscosity of the B100 fuel (4.99 cSt/s at 40°C) was slightly higher than would be assumed based solely on the FAME composition profile, suggesting that there were some unreacted species still present in the fuel.
3.2. CO2 Emissions
Figure 1 shows the fuel-specific emissions of CO2 from both the generator and mower engines as a function of biodiesel content. Both engines showed a consistent decrease in CO2 with increasing biodiesel content. Raw CO2 exhaust concentrations, however, did not vary significantly for either engine between the different fuels. The observed decrease in fuel-specific CO2 emissions is due to the increased oxygen content in the biodiesel fuels, which results in a higher MWfuel value for higher biodiesel blends. At the same time, however, the energy content of a 100% biodiesel fuel is also 9-10% lower than that of petroleum diesel [6]. This will result in increased fuel consumption for the same engine power output with biodiesel blends, offsetting any decrease in CO2 emissions. In our results, fuel-specific CO2 emissions decreased by 10% and 10.5%, respectively, for the generator and mower engines with B100, so total emissions on a power-specific basis would not show any significant change. In general, biodiesel fuels are not typically expected to have a significant effect on exhaust CO2 emission rates. Biodiesel may, however, be more carbon neutral overall because of the carbon source (biological versus fossil carbon). Determining the actual net CO2 emissions difference due to biodiesel blending requires a lifecycle emissions analysis for the specific fuel that is beyond the scope of this paper.
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3.3. Generator Emissions
Figure 2 shows the average emissions for CO, , and total hydrocarbons (THC) from the generator for the different fuel blends. Carbon monoxide and total hydrocarbon emissions decreased by 46 and 68%, respectively, between the number 2 diesel and B100 fuels. The majority of this decrease occurred between 0 and 20% biodiesel content, with further increases in biodiesel content having a much smaller incremental effect on emissions of both compounds. Total nitrogen oxides, on the other hand, increased with greater biodiesel content, with the greatest change also occurring between the B5 and B20 blends. These results suggest that the largest impact on the combustion process is achieved at relatively low oxygen content in the fuel (1-2%). In engines of this type, biodiesel blends at or below 5% would thus have minimal impact on exhaust emissions, while blends with more than 20% biodiesel content will all have relatively similar emissions profiles. As most engines are not optimized for idling conditions, total emissions will likely decrease at higher engine speeds, reducing the absolute differences between different fuels.
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The fuel-specific emissions reported here do not account for any changes in fuel consumption rates related to the lower energy content of the biodiesel blends. This is due to the difficulty in accurately measuring output power at “no load” conditions. However, the effect of these changes can be estimated. For a 10% decrease in energy content between the petroleum diesel and the B100 fuel, we estimate a 10% increase in fuel consumption to achieve the same power output. This would also increase total emissions of all constituents by 10% on a brake-specific basis (g fuel/power × time; e.g., g/kWh). As the changes in fuel-specific emissions for CO, THC, and NO are substantially larger than 10%, these constituents will be reduced (or increased, for NO) even after accounting for increased fuel consumption.
The higher bulk modulus of compressibility of biodiesel fuels can result in advanced fuel injection timing by as much as one to two crank-angle degrees [35, 36]. Additionally, changes in the spray and mixing behavior from oxygen content and fuel stoichiometry can increase the local temperature and heat release in the autoignition zone of the flame [27]. Both of these factors will result in a hotter combustion process as the biodiesel content of the fuel increases. In turn, this should result in more complete combustion, and a corresponding decrease in carbon monoxide and total hydrocarbon emissions, as seen in our results. The increased emissions are due to a combination of several different factors including advanced combustion and a hotter burn [25, 27, 37]. These conditions result more time at increased in-cylinder temperatures, which can promote increased production through the thermal NO mechanism.
Results from the ANOVA analysis of the generator emissions data showed that the fuel biodiesel content was significantly correlated to changes in emissions of all compounds except for NO2. Nitrogen dioxide formation and destruction reactions will both be influenced by biodiesel-induced changes in combustion temperature and timing. Overall, we observed no consistent net effect due to the presence of biodiesel in the fuel. Variations in ambient temperature and humidity in the test cell were small during these tests (temperatures from 22–24°C and humidity from 55–60 grains/lb dry air) and did not impact the exhaust composition, while the exhaust temperature was significantly correlated with CO2 concentrations only. The measured exhaust temperature did decrease with higher biodiesel content, from a high of 106°C with number 2 diesel to a low of 98°C with the B100 fuel, a change directly related to the advanced injection timing. While biodiesel may burn hotter during the combustion process, this combustion occurs earlier in the expansion stroke of the engine. Since combustion is completed closer to top dead center, more work can be done by the engine (longer effective expansion stroke) before the exhaust valve opens and the cylinder walls see a larger temperature gradient for a longer time, promoting convective heat transfer. As a result, the exhaust temperature will decrease even though the peak combustion temperature is higher.
3.4. Mower Emissions
The effect of biodiesel blending on exhaust emissions of CO, THC, and was substantially different for the mower engine (Figure 3). While total hydrocarbon emissions did decrease with increasing biodiesel content, the change was not significant except for the B100 fuel. The maximum reduction of 25% from the B5 to the B100 fuel was also much smaller than the 52% reduction between the same two fuels in the generator studies. CO emissions showed no consistent pattern as biodiesel content increased, despite the typical linkage between these two partial combustion products.
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emissions, by contrast, declined with increasing biodiesel content, with the greatest change between 50% and 100% biodiesel. This trend was very similar to that observed for total hydrocarbon emissions. NO was also a substantially higher fraction of total emissions from the mower, accounting for more than 75% of recorded , as compared to 46–52% from the generator. The fuel-specific results from the mower study can also be adjusted to account for changes in biodiesel energy content, using the approach outlined above for the generator results. The decrease in both and THC concentrations was greater than the expected rate of increased fuel consumption for the B100 fuels, so emission reductions would occur for both compounds on a brake-specific basis as well. As with the generator engine, emissions may be more similar for the different fuel blends at higher operating speeds.
The ANOVA results for the mower study indicate that changes in fuel biodiesel content are significantly correlated with changes in emissions of all measured compounds, including NO2 (although the absolute changes in NO2 emissions were very small). Exhaust temperature was correlated with CO2, NO, and THC, but not with CO and NO2. The overall range of exhaust temperatures was smaller in the mower studies, with a maximum of 84°C during the B5 tests and a minimum of 81°C with B100. Ambient conditions also varied more during the mower tests, which were conducted outdoors. Temperatures during these tests ranged from 13–27°C and humidity from 23–73 grains/lb dry air. Even so, ANOVA regression indicated no significant effect for ambient temperature on emission results. Humidity, however, was correlated with changes in CO2, CO, and NO2 emissions. Changes in humidity can affect the fuel viscosity, which can in turn affect fuel injection and combustion patterns, resulting in fluctuations in CO and CO2 emissions. Increased humidity in the intake air has also been shown to decrease total production in multiple previous studies [38–40]. We used correction factors available for naturally aspirated off-road diesel engines [41] to adjust our results for the effects of humidity by calculating reference values for each biodiesel content that were independent of ambient conditions. These adjusted data produced a similar trend in total emissions to the uncorrected results.
3.5. Comparing Biodiesel Effects on Exhaust Emissions
Fuel-specific emissions for all pollutant compounds except for CO were much higher from the mower in comparison to the generator at all biodiesel contents (Figures 2 and 3). Most notably, total concentrations were four to five times higher (70 g/kg fuel at 5% biodiesel content, compared to 15 g/kg fuel from the generator), with the majority of this difference due to increases in NO. As noted above, trends for some compounds were also notably different as the biodiesel content increased. Table 5 provides the results of the Pearson correlation analysis between the significant influence factors (as determined by ANOVA analysis) and pollutant emissions levels. The major difference with respect to biodiesel content, the only factor significant for both engines, is with nitric oxide emissions, which decreased for the mower but increased for the generator as the biodiesel content increased. Additionally, CO emissions were only linearly correlated with biodiesel content for the generator.
The generator and front mower used in this experiment represent two different engine designs with respect to their fuel injection control. The US EPA adopted off-road diesel engine emissions regulations for engines under 50 hp in 1996, after the front mower was put into service. The mower engine would therefore have had a fuel injection system optimized for performance at the expense of emission control. The generator, by contrast, was built in 2007 and therefore subject to Tier 2 emissions standards for engines under 11 hp [29]. After off-road emissions standards were introduced, engine manufacturers began retarding the injection timing away from an optimum situation in order to reduce combustion temperatures and prevent the formation of , a regulated compound. Moreover, increased levels of Exhaust Gas Recirculation (EGR) were introduced to act as a thermal diluent effectively reducing the combustion temperature. Hence, the generator has a port in the cylinder head that allows flow of exhaust gases from the exhaust manifold to the intake. This mower does not appear to have a dedicated EGR system (http://golftechs.us/Manuals/JD220dieselengine.pdf); since emission regulations did not exist at the time of its manufacture and EGR can decrease the fuel economy of the engine, there would be no reason to include such a system.
This difference in injection timing is the most likely source for the different responses of the two engines to increased biodiesel content. Retarding the combustion process will produce lower overall formation as combustion occurs more in the expansion stroke within a relatively “cooler” environment. NO2 is formed quickly from NO in a hot environment and can also be destroyed quickly, provided temperatures remain elevated. While NO2 can form rapidly in both engines, the flame quenches more easily in the generator, removing the necessary energy to convert NO2 back to NO. This accounts for the higher ratio of NO to NO2 in the mower at all fuel compositions.
Increasing the fuel biodiesel content should result in an accelerated fuel injection sequence in both the generator and mower engines, as discussed previously. The change in injection timing, however, may have a much less significant effect on the combustion profile for the older mower engine. When fuel injection timing is optimized for performance, heat release is maximized closer to top dead center, when the piston is moving relatively slowly. Hence, changing by a few crank-angle degrees will have a smaller effect on conditions within the cylinder. Under these conditions, the lower energy content of biodiesel may play a more important role in nitrogen oxide formation by reducing the in-cylinder temperature, resulting in the decreased B100 emissions observed in the front mower. The corresponding reduction in total hydrocarbon emissions in this fuel would thus be due primarily to the chemical composition of the WCO biodiesel, which allows for more complete fuel combustion even at slightly reduced temperatures. For the generator engine, by contrast, changing a few crank angle degrees for combustion can have a large effect on exhaust emissions, as pressures and temperatures are changing more dramatically during the expansion stroke (the piston accelerates from top dead center to the middle of the expansion stroke). Further investigation of this behavior would require collection of in-cylinder pressure and temperature data, which was not available for this study.
4. Conclusions
While the physical properties of the six WCO biodiesel batches produced by the KU Biodiesel Initiative showed little variation, the FAME content of the four samples collected in 2010 included less saturated compounds while consisting of longer chain compounds than the 2009 samples. Elemental analysis of the fuel H : C ratio and oxygen content were generally in line with the FAME analysis, indicating that the GC-MS technique provided a good characterization of the overall fuel, despite the presence of some unquantifiable fragments. The small differences in fuel batch-to-batch variability suggest that changes in the WCO feedstock makeup will have relatively little effect on the resulting fuel.
Increased WCO biodiesel content in the fuel lowered emissions of total hydrocarbons in both engines under idle conditions, with greater reductions at lower biodiesel content in the generator engine. These decreases are consistent with similar results from other studies of waste cooking oil biodiesel and most likely result from compositional differences between biodiesel and petroleum diesel, particularly the higher oxygen level and lower aromatic content. The relationship between biodiesel content and CO and emissions, by contrast, varied substantially between the two engines. The generator results follow typical patterns in the literature for biodiesel, with decreased CO and increased production. In the front mower, however, increased biodiesel content resulted in decreased emissions and had virtually no effect on CO. This difference is likely related to differences in fuel injection timing strategies between the two engines.
These results indicate that the effects of biodiesel use in nonroad engines on emission profiles may depend greatly on the fuel injection strategy used, which in turn will be related to the age of the engine. In the United States, off-road vehicles and equipment less than 10–15 years old (depending on the specific engine class) are subject to the U.S. EPA’s tiered emissions standards for off-road engines. As a result, these engines will generally employ delayed fuel injection timing to control emissions, along with EGR, and may see increased and reduced hydrocarbon emissions due to biodiesel use. Engines built before this time, however, were not subject to emission regulations, and are more likely to be optimized for engine performance. Many stationary diesel engines currently in use will also fall into this category, as regulations for these engines apply only to new engines built since 2007.
Our results suggest that the use of biodiesel blends in these older off-road and stationary engines may actually result in the reduction of both and total hydrocarbon emissions levels. As our studies were conducted only under idle conditions and for one type of biodiesel fuel, they must be considered preliminary, and more testing on older off-road diesel engines should be conducted to determine the full nature and extent of this effect. If this pattern is observed for a broader range of conditions, however, then the use of biodiesel blends in preemissions control off-road engines could have a substantially positive effect on exhaust emissions of gas-phase pollutants.
Acknowledgments
The authors thank Pavan Ilipilla of the University of Kansas Environmental Engineering program for assistance in data collection. This research was funded by the University of Kansas, Transportation Research Institute from Grant no DT0S59-06-G-00047, provided by the U.S. Department of Transportation Research and Innovative Technology Administration.