Performance Analysis of a Compression Ignition Engine Using Mixture Biodiesel Palm and Diesel
Abstract
1. Introduction
2. Materials and Methods
2.1. Selection of Control Variables
2.2. Selection of Analysis Method
2.3. Instrumentation
3. Run Test
Control Mechanisms
4. Experimental Design
Experimental Test
5. Results
6. Conclusions
- From the initial measurements with the test bench where the performance evaluation of the engine was performed using diesel-biodiesel mixture working under the conditions of 1800 rpm and a load percentage of 35%, 50%, 65% and 80%, it was determined that the statistical means of the data presented differences in the analysis ANOVA p = 0.47, therefore p > 0.05 and p < Fcrit where F = 0.92 and Fcrit = 4.06 establish that the measured values have no significant relationship and significative variation of the data. This is due to the increase in temperature inside the cylinder, allowing the engine to get closer to the area of lower consumption or higher performance. However, at low speed the fuel consumption increases due to the higher rate of heat transfer through the walls.
- The implementation of the mechanisms of attenuator of air blows, adjustment mechanism for rpm and preheating air chamber for intake manifold allowed us to improve the bench of tests and improve the measurement of the variables fuel, air, oil temperature, exhaust gas temperature and torque. Emissions were statistically significant with values and only the rpm with showed a statistically insignificant value. These results were due to the instability in the combustion of the 912 cc HATZ engine.
- This HATZ engine does not have the common rail system, which is an electronic system of fuel injection, which supplies diesel by using a high-pressure pump to a common duct where all the injectors are connected. Therefore, the mechanical improvements reduced the variability in the measured data. This did not guarantee the statistical reproducibility of the experiment, but did obtain repeatability in the test.
- The ANOVA analysis of multiple linear regression and Pearson correlation allowed for identifying the emissions variables with the highest correlation in the FC, CO2 = 0.791, O2 = −0.768 and NOx = 0.72 indicating high correlation and a significant linear relationship; the air consumption with HC = 0.447 and NOx = −0.441 showed a medium correlation with CO, while showing a very low correlation with CO2 and O2 variables. For the gas temperatures with CO2 = 0.857, O2 = −0.847 and NOx = 0.870, NOx is the only variable that has a significant linear relationship with the temperature of the gases.
- The elements used in the improvement of the test bench allow better control over the variables of interest to determine the performance of the engine. Humidity and temperature were only partially controlled, which affects the statistical result. These experiments were conducted order to determine the performance of diesel-biodiesel engines reliably and accurately in Colombia, where palm oil is produced as an energy product.
Author Contributions
Funding
Acknowledgments
Conflicts of Interest
References
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| Properties | Density at 15 °C gm/ml | Kinematic Viscosity at 40 °C mm2/s | Flash Point, °C | Heating Value MJ/kg |
|---|---|---|---|---|
| Method | ASTM D1298 | ASTM D445 | ASTM D92 | ASTM D270 |
| B100 | 0.877 | 4.56 | 196 | 40.56 |
| Palm oil | 0.925 | 41 | 260 | 39.849 |
| Properties | B10 |
|---|---|
| Higher calorific power (MJ/kg) | 45.4 |
| Lower calorific power (MJ/kg) | 42.9 |
| Specific gravity (a 20 °C) | 0.87 |
| Flash point (°C) | 60 |
| Freezing point (°C) | 23 |
| Cloud point (°C) | 45 |
| Soot (%) | 0.001 |
| Cetane number (Cst) | 45-50 |
| Viscosity (20 °C) (Cst) | 4.1 |
| Viscosity (40 °C) (Cst) | 2.6 |
| Viscosity (60 °C) (Cst) | 2.046 |
| Viscosity (100 °C) (Cst) | 1.1 |
| Variable | Units |
|---|---|
| Engine speed | Revolutions per minute (rpm) |
| Torque | N-m |
| Fuel consumption | mg/s |
| Air consumption | /h |
| Exhaust gases temperature | °C |
| Motor oil temperature | °C |
| Carbon monoxide | CO |
| Carbon dioxide | CO2 |
| Hydrocarbons | HC |
| Nitrogen oxides | NOX |
| Oxygen | O2 |
| Source of Variance | Sum of Squares | Degrees of Freedom (df) | Mean Squares (SS/df) | F-ratio (F statistic) | Sig. |
|---|---|---|---|---|---|
| Regression | Regression SS | 1 | Regression MS | F | Pr(F>Fobs) |
| Residual | Residual SS | N-k | Residual MS | ||
| Total | SST | N-1 |
| Parameter | Measurement Interval (normalized) |
|---|---|
| Maximum flow range | 0.05 to 200 Nm/s air velocity at standard conditions 100 psi |
| Minimum flow range | 0.05 to 2.5 Nm/s air velocity at standard conditions 100 psi |
| Precision | +/−1% Reading |
| Repeatability | +/−0.5% Reading |
| Working temperature | 70 to 40 °C |
| Measurement Range | 0–2500 ppm |
|---|---|
| Operating temperature | 5 to 45 °C |
| Response time | T90 in 30 s |
| Linearity | +/−2% of full scale |
| Reproducibility | +/−0.5% of full scale |
| Warm-up time | 30 min |
| Analog out | 0–1 V |
| Measurement Parameters | Unit | Range | Resolution |
|---|---|---|---|
| Turning rate | rpm | 250 to 800 | 10 |
| Oil temperature | °C | 1 to 120 | 1 |
| CO | % vol. | 0 to 10 | 0.01 |
| CO2 | % vol. | 0 to 20 | 0.1 |
| HC | **ppm in vol. | 0 to 20000 | 1 |
| O2 | % vol. | 0 to 4 and 4 to 22 | 0.01 0.1 |
| NO | **ppm in vol. | 0 to 9000 | 1 |
| Spark advance angle * | ° of the crankshaft | −10 to 100 | 0.1 |
| Parameter | Units | Measurement Range | Resolution |
|---|---|---|---|
| Rotation | rpm | 250 to 800 * | 10 |
| Oil temperature | °C | 1 to 120 * | 1 |
| Load | Regime (rpm) | Torque (Nm) | Fuel | Air | Exhaust Gases Temp | Oil Temp | NOx | CO | CO2 | O2 | HC | ||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Load | Desired | Measured | Desired | Measured | mg/s | N*m3/h | °C | °C | ppm | % Vol | % Vol | % Vol | ppm |
| 35% | 1800 | 1805 | 17.5 | 17.39 | 228 | 123.1 | 197.26 | 79 | 463 | 0.07 | 3.4 | 16.1 | 33 |
| 1800 | 1820 | 17.5 | 18.11 | 219 | 120.13 | 179.27 | 83 | 475 | 0.07 | 3.8 | 15.7 | 39 | |
| 1800 | 1812 | 17.5 | 17.69 | 216 | 120.08 | 191.46 | 98 | 448 | 0.06 | 3.7 | 15.7 | 38 | |
| 50% | 1800 | 1815 | 25 | 25.20 | 315 | 106.24 | 254.80 | 93 | 784 | 0.05 | 5.0 | 13.9 | 47 |
| 1800 | 1802 | 25 | 25.60 | 298 | 107.12 | 252.50 | 93 | 774 | 0.06 | 5.1 | 13.9 | 49 | |
| 1800 | 1820 | 25 | 25.05 | 290 | 110.51 | 251.50 | 106 | 890 | 0.06 | 5.3 | 13.5 | 31 | |
| 65% | 1800 | 1811 | 32 | 32.01 | 348 | 115.08 | 310.00 | 104 | 1061 | 0.10 | 6.6 | 11.6 | 45 |
| 1800 | 1791 | 32 | 32.10 | 345 | 109.66 | 307.00 | 104 | 1326 | 0.12 | 6.8 | 11.2 | 59 | |
| 1800 | 1824 | 32 | 31.69 | 356 | 114.41 | 313.56 | 114 | 1133 | 0.09 | 6.5 | 11.7 | 44 | |
| 80% | 1800 | 1787 | 40 | 41.50 | 487 | 118.87 | 422.69 | 111 | 1485 | 0.52 | 9.0 | 7.9 | 63 |
| 1800 | 1790 | 40 | 41.25 | 482 | 119.32 | 422.11 | 112 | 1478 | 0.52 | 8.9 | 8.0 | 64 | |
| 1800 | 1815 | 40 | 40.90 | 488 | 115.42 | 424.00 | 114 | 1526 | 0.47 | 8.9 | 8.0 | 72 | |
| F value | P value | Fcrit | |
|---|---|---|---|
| CO (%vol) | 2.016 | 0.073 | 2.216 |
| CO2 (%vol) | 12.749 | 1.687 × 10 −7 | 2. 216 |
| O2 (%vol) | 13.336 | 1.091 × 10 −7 | 2. 216 |
| HC (ppm) | 3.063 | 0.010 | 2. 216 |
| NOx (ppm) | 19.325 | 2.607 × 10 −9 | 2. 216 |
| TORQUE (N.m) | 4.655 | 7.988 × 10 −4 | 2. 216 |
| RPM | 0.632 | 0.784 | 2. 216 |
| GAS TEMP (°C) | 68.026 | 2.430× 10 −15 | 2. 216 |
| AIR CONSUM (m3/h) | 48.692 | 1.102× 10 −13 | 2. 216 |
| EXHAUST GASES TEMP (°C) | 50.680 | 7.009× 10 −14 | 2. 216 |
| OIL TEMP (°C) | 7.316 | 2.531× 10 −5 | 2. 216 |
| Fuelcons | CO | CO2 | O2 | HC | NOx | |
|---|---|---|---|---|---|---|
| Fuelcons | 1.000 | 0.278 | 0.791 | −0.768 | −0.542 | 0.720 |
| CO | 0.278 | 1.000 | 0.532 | −0.538 | 0.155 | 0.466 |
| CO2 | 0.791 | 0.532 | 1.000 | −0.994 | −0.392 | 0.972 |
| O2 | −0.768 | −0.538 | −0.994 | 1.000 | 0.351 | −0.972 |
| HC | −0.542 | 0.155 | −0.392 | 0.351 | 1.000 | −0.437 |
| NOx | 0.720 | 0.466 | 0.972 | −0.972 | −0.437 | 1.000 |
| Model | R | R Square | R Adjusted Square | Standard Error of the Estimate | Statistic change | ||||
|---|---|---|---|---|---|---|---|---|---|
| Change in R Square | Change in F | df1 | df2 | Sig. change in F | |||||
| 1 | 0.791a | 0.625 | 0.614 | 27.341 | 0.625 | 56.662 | 1 | 34 | 0.000 |
| 2 | 0.830b | 0.689 | 0.670 | 25.275 | 0.064 | 6.786 | 1 | 33 | 0.014 |
| 3 | 0.876c | 0.768 | 0.746 | 22.188 | 0.079 | 10.819 | 1 | 32 | 0.002 |
| Model | Sum of square | df | Mean squares | F | Sig. | |
|---|---|---|---|---|---|---|
| 1 | Regression | 42357.948 | 1 | 42357.948 | 56.662 | 0.000b |
| Residue | 25416.940 | 34 | 747.557 | |||
| Total | 67774.889 | 35 | ||||
| 2 | Regression | 46693.167 | 2 | 23346.583 | 36.545 | 0.000c |
| Residue | 21081.722 | 33 | 638.840 | |||
| Total | 67774.889 | 35 | ||||
| 3 | Regression | 52019.993 | 3 | 17339.998 | 35.220 | 0.000d |
| Residue | 15754.896 | 32 | 492.340 | |||
| Total | 67774.889 | 35 | ||||
| b: CO2, c: CO2, HC, d: CO2, HC, NOx | ||||||
| TempGases | CO | CO2 | O2 | HC | NOx | ||
|---|---|---|---|---|---|---|---|
| Pearson correlation | TempGases | 1.000 | 0.424 | 0.857 | −0.847 | −0.497 | 0.870 |
| CO | 0.424 | 1.000 | 0.532 | −0.538 | 0.155 | 0.466 | |
| CO2 | 0.857 | 0.532 | 1.000 | −0.994 | −0.392 | 0.972 | |
| O2 | −0.847 | −0.538 | −0.994 | 1.000 | 0.351 | −0.972 | |
| HC | −0.497 | 0.155 | −0.392 | 0.351 | 1.000 | −0.437 | |
| NOx | 0.870 | 0.466 | 0.972 | −0.972 | −0.437 | 1.000 | |
| Model | R | R Square | R Adjusted Square | Standard Error of the Estimate | Statistic Change | ||||
|---|---|---|---|---|---|---|---|---|---|
| Change in R Square | Change in F | df1 | df2 | Sig. Change in F | |||||
| 1 | 0.870a | 0.756 | 0.749 | 15.553 | 0.756 | 105.365 | 1 | 34 | 0.000 |
| Model | Sum of Square | df | Mean Squares | F | Sig. | |
|---|---|---|---|---|---|---|
| 1 | Regression | 25489.332 | 1 | 25489.332 | 105.365 | 0.000b |
| Residue | 8225.135 | 34 | 241.916 | |||
| Total | 33714.467 | 35 | ||||
| b: NOx | ||||||
| Aircons | CO | CO2 | O2 | HC | NOx | |
|---|---|---|---|---|---|---|
| Aircons | 1.000 | −0.138 | −0.294 | 0.284 | 0.447 | −0.441 |
| CO | −0.138 | 1.000 | 0.532 | −0.538 | 0.155 | 0.466 |
| CO2 | −0.294 | 0.532 | 1.000 | −0.994 | −0.392 | 0.972 |
| O2 | 0.284 | −0.538 | −0.994 | 1.000 | 0.351 | −0.972 |
| HC | 0.447 | 0.155 | −0.392 | 0.351 | 1.000 | −0.437 |
| NOx | −0.441 | 0.466 | 0.972 | −0.972 | −0.437 | 1.000 |
| Model | R | R Square | R Sum of Square | Standard Error of the Estimate | Statistic Change | ||||
|---|---|---|---|---|---|---|---|---|---|
| Change in R Square | Change in F | df1 | df2 | Sig. Change in F | |||||
| 1 | 0.447a | 0.200 | 0.177 | 1.566 | 0.200 | 8.509 | 1 | 34 | 0.006 |
| Model | Sum of Square | df | Mean Squares | F | Sig. | |
|---|---|---|---|---|---|---|
| 1 | Regression | 20.882 | 1 | 20.882 | 8.509 | 0.006b |
| Residue | 83.440 | 34 | 2.454 | |||
| Total | 104.321 | 35 | ||||
| b: HC | ||||||
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Vargas, F.; Pérez, A.; Delgado, R.; Hernández, E.; Suástegui, J.A. Performance Analysis of a Compression Ignition Engine Using Mixture Biodiesel Palm and Diesel. Sustainability 2019, 11, 4918. https://doi.org/10.3390/su11184918
Vargas F, Pérez A, Delgado R, Hernández E, Suástegui JA. Performance Analysis of a Compression Ignition Engine Using Mixture Biodiesel Palm and Diesel. Sustainability. 2019; 11(18):4918. https://doi.org/10.3390/su11184918
Chicago/Turabian StyleVargas, Fabián, Armando Pérez, Rene Delgado, Emilio Hernández, and José Alejandro Suástegui. 2019. "Performance Analysis of a Compression Ignition Engine Using Mixture Biodiesel Palm and Diesel" Sustainability 11, no. 18: 4918. https://doi.org/10.3390/su11184918
APA StyleVargas, F., Pérez, A., Delgado, R., Hernández, E., & Suástegui, J. A. (2019). Performance Analysis of a Compression Ignition Engine Using Mixture Biodiesel Palm and Diesel. Sustainability, 11(18), 4918. https://doi.org/10.3390/su11184918

