Attasit Wiangkhama,
Niti Klinkaewb,
Prasert Aengchuanc,
Pansa Liplapd,
Atthaphon Ariyarite and
Ekarong Sukjit*e
aDepartment of Industrial Engineering, Faculty of Engineering, Srinakharinwirot University, Ongkharak, Nakhon Nayok 26120, Thailand
bInstitute of Research and Development, Suranaree University of Technology, Muang, Nakhon Ratchasima 30000, Thailand
cSchool of Manufacturing Engineering, Institute of Engineering, Suranaree University of Technology, Muang, Nakhon Ratchasima 30000, Thailand
dSchool of Agricultural Engineering, Institute of Engineering, Suranaree University of Technology, Muang, Nakhon Ratchasima 30000, Thailand
eSchool of Mechanical Engineering, Institute of Engineering, Suranaree University of Technology, Muang, Nakhon Ratchasima 30000, Thailand. E-mail: ekarong@sut.ac.th
First published on 24th August 2023
This study investigates the impact of adding diethyl ether (DEE) to pyrolysis oil derived from mixed plastic waste on engine performance, combustion characteristics, and emissions. The blending of different DEE concentrations (5%, 10%, and 15% by volume) with waste plastic oil (WPO) was analyzed. Experiments were conducted on a four-cylinder diesel engine, varying engine loads while maintaining engine speed. The results indicate that WPO mainly comprises middle-distillate hydrocarbons (52.58% C13–C18 and 26.15% C19–C23). While WPO had lower specific gravity, density, and flash point, it met diesel fuel specifications for kinematic viscosity and cetane index. The addition of DEE led to decreased properties in all blended fuels, except for the cetane index. Engine performance declined with WPO–DEE blends at low engine loads but improved at high engine loads with minimal variation as DEE concentration increased. DEE addition resulted in a shorter ignition delay and earlier combustion, although increasing DEE concentration did not further advance combustion. NOx emissions significantly decreased with DEE addition, while HC and CO emissions remained unaffected at high engine loads. To optimize the process, the non-dominated sorting genetic algorithm II (NSGA-II) with generalized regression neural networks (GRNNs) was employed as a surrogate multi-objective function. The GRNNs model demonstrated excellent performance, achieving high R2 values of 0.952 and 0.918, low RMSE values of 0.659 and 0.310, and MdAPE values of 2.675% and 5.098% for brake thermal efficiency (BTE) and NOx, respectively. The NSGA-II algorithm with GRNNs model proved successful in predicting the multi-objective function in the optimization process, even with limited data. The Pareto frontier analysis revealed an optimal DEE percentage of approximately 10% to 14% for maximum BTE and minimum NOx, with engine loads distributed around 30, 40, and 100 N m.
In Thailand, waste disposal is currently managed by burying it in designated areas to minimize air pollution impact. However, the proximity to the equator leads to challenges during the rainy season, causing chemicals, dangerous organic matter, and heavy metals to seep into the soil beneath the buried waste. Similarly, during the summer season, liquid within the buried waste can evaporate and be released into the atmosphere. Proactive waste disposal measures are critical to prevent environmental harm. Despite government efforts to reduce plastic consumption and promote recycling, the quantity of plastic waste continues to surge.3 Pyrolysis has emerged as a potential solution to convert plastic waste into fuel oil similar to diesel.4–7 This thermal degradation process occurs in an oxygen-free environment at elevated temperatures, producing liquid, gaseous, and solid products, influenced by feedstock composition and pyrolysis parameters.7 The fuel properties of waste plastic pyrolysis oils (WPO) vary based on plastic sources,8–10 with significant differences observed in kinematic viscosity, flash point, and cetane index compared to diesel fuel. However, the higher density and cetane number of WPO contribute to improved air–fuel mixing, despite its lower flash point. These findings have implications for its potential use as a transportation fuel.
The engine test results revealed that the brake thermal efficiency (BTE) of the waste plastic oil (WPO) was lower than that of diesel fuel, attributed to its high viscosity and poor atomization, resulting in inadequate mixture formation during the premixed combustion phase.4,5,11 Conversely, using WPO achieved a higher BTE compared to diesel fuel, primarily due to WPO's higher cetane number, which promoted better air–fuel mixing.6,12,13 Prior research indicated that during combustion, WPO generated a lower in-cylinder pressure (ICP) than diesel fuel, attributed to ignition delay. However, the heat release rate (HRR) from WPO was higher than that of diesel fuel, owing to WPO's greater compressibility, leading to a more efficient fuel injection during the combustion process.6,12 On the other hand, some scholars argued that both ICP and HRR of WPO were higher than those of diesel fuel.14 This could be attributed to WPO's high viscosity and low volatility, resulting in a delay in the preparation of an air–fuel mixture and a sudden surge in cylinder pressure during the premixed combustion phase. Additionally, WPO's higher calorific value and lower atomization during premixed combustion may be responsible for the higher HRR.4,5,13 Compression ignition engines are known to emit two primary pollutants: particulate matter (PM) and oxides of nitrogen (NOx). PM is a hazardous substance that can cause respiratory and dermal problems in the short and long term, as documented in previous research.15 NOx is a gas identified as a contributor to acid rain.16 The generation of PM in engines is associated with the combustion of fuels containing C–C chemical compounds, such as diesel fuel.17 Some researchers6,12 reported that using WPO as engine fuel resulted in reduced smoke emission, an indicator of PM levels. This reduction was attributed to WPO's high cetane index, leading to a more optimal air–fuel mixture and cleaner combustion. However, other studies reported an increase in smoke emission when using WPO due to its low cetane index.4,5,11
Numerous researchers have extensively investigated the utilization of oxygenated fuels, such as biodiesel and ethanol, as potential solutions for reducing PM and NOx emissions from diesel engines. While these fuels have demonstrated effectiveness in reducing PM emissions, their use often leads to an increase in NOx emissions due to the higher oxygen content, which promotes higher combustion temperatures, favorable for NOx formation. This finding has been consistently documented in various studies.4–6,11–13,17–20 Several studies have specifically highlighted the benefits of using butanol, an oxygenated fuel with a higher oxygen content than ethanol, in reducing PM emissions when blended with diesel fuel.21,22 Additionally, the use of biodiesel blends has been found to result in lower PM emissions compared to regular diesel fuel.13 However, when researchers investigated the use of diesel-diethyl ether blends or diethyl ether (DEE) as a supplemental fuel, they found that while PM emissions decreased due to reduced carbon content in the fuel, NOx emissions increased due to the higher oxygen content leading to elevated combustion temperatures.6,19,20,23,24 Based on the findings reported in previous publications, blending WPO with butanol and DEE resulted in a decrease in BTE and an increase in brake specific fuel consumption (BSFC) primarily due to the lower heating value of butanol and DEE.4,6 However, the addition of biodiesel to the blended fuel led to an increase in BTE and a decrease in BSFC, likely attributed to the higher heating value and favorable combustion characteristics of the fuel.13 Regarding combustion characteristics, the WPO–DEE blend exhibited lower in-cylinder pressure (ICP) and heat release rate (HRR) compared to diesel fuel due to ignition delay. However, when 5.5% v/v biodiesel was added to the blend, the ICP and HRR approached values closer to those of neat WPO. Moreover, the inclusion of biodiesel in the blend resulted in a significant decrease in unburned hydrocarbon (HC) and carbon monoxide (CO) emissions at low engine load.6 DEE is a chemical compound with the molecular formula C4H10O, and it can be obtained through the dehydration reaction of ethanol. One of its notable properties is an exceptionally high cetane number, which indicates its effectiveness in promoting air–fuel mixing within the combustion chamber, surpassing that of diesel fuel.6,19,20,23,24 Thailand's agricultural sector is characterized by extensive cultivation of crops, with a primary focus on those rich in starch content. This abundance of starch-based crops presents an opportunity for ethanol production. Additionally, the sugar production industry in Thailand generates molasses, which can also be harnessed for ethanol production. Consequently, Thailand possesses sustainable resources for DEE production, with all feedstocks originating from the agricultural sector.
Numerous research studies have been dedicated to exploring alternative and renewable fuels derived from agricultural and municipal solid wastes, recognizing their potential for sustainability and their capacity to mitigate greenhouse gas emissions and other pertinent environmental impacts.25–29 These investigations have delved into the efficiency and emissions of engines fueled with such alternative fuels and blends, considering various parameters such as fuel type, engine load, compression ratio, fuel injection pressure, and fuel injection timing.30–32 The engine's performance has been comprehensively evaluated in terms of BTE, BSFC, and emissions including NOx, HC, CO, and black smoke, all of which are critical factors in environmental protection. Moreover, these studies have sought to determine the optimal conditions for blended fuels and engine operating parameters, employing optimization algorithms to achieve the highest engine efficiency while minimizing emissions.33–35 In the optimization process, the objective function, serving as a surrogate for the relationship between input and output factors in optimization problems, plays a crucial role.36 In recent times, artificial intelligence models have emerged as powerful tools for serving as objective functions or surrogate models due to their high accuracy in predicting the behavior of outputs based on problem inputs.37,38 Among the widely used algorithms in renewable energy-related problems, the neural network model, inspired by human learning behavior, stands as one of the most commonly employed.39–41
The objective of this research is to analyze the impact of blending diethyl ether into waste plastic oil concerning fuel blending ratio and engine operating conditions, with a focus on engine performance, combustion characteristics, and engine-out emissions. Additionally, the study aims to identify the optimal blended diethyl ether ratio and engine operating conditions that achieve both high engine efficiency and minimal emissions. To attain these research objectives, the non-dominated sorting genetic algorithm II (NSGA-II) was employed, a widely-used approach in multi-objective optimization. Furthermore, the study utilized generalized regression neural networks (GRNNs), a type of neural network model known for its suitability in handling small data sets and delivering high prediction performance, to serve as a surrogate for the multi-objective function during the optimization process.42,43
The WPO–DEE blended fuel was prepared by mixing using a magnetic stirrer at room temperature for 15 minutes. The DEE-to-WPO blend ratio was varied at 5%, 10% and 15% by volume and named DEE5, DEE10 and DEE15, respectively. All fuel properties and test standards are presented in Table 1. The table illustrates that the specific gravity, density and flash point of the WPO are lower than the standard diesel fuel, while the kinematic viscosity and cetane index are within the range of diesel fuel specifications. In all blended fuels, the properties decreased when DEE was added, as DEE has lower properties compared to diesel fuel. Nevertheless, the cetane index of the blended fuels was higher than that of diesel fuel due to the significantly higher cetane index of DEE. It is observed that the flash point of the resulting WPO is comparatively lower than that of diesel fuel. Moreover, as the concentration of DEE in the blend increases, the flash point of the blend decreases continuously. Given that low flash point fuels are more susceptible to combustion, extra precautions are necessary to prevent accidental ignition and potential fires. To ensure safe handling and usage of WPO blended with DEE, it is imperative to implement appropriate safety measures, including the use of proper storage containers. These measures will contribute to minimizing potential risks associated with the handling of such fuel blends.
Fuel properties | ASTM test method | Test fuels | |||||
---|---|---|---|---|---|---|---|
Diesel | WPO | DEE | DEE5 | DEE10 | DEE15 | ||
Kinematic viscosity@40 °C (cSt) | D445 | 3.44 | 3.065 | 0.240 | 2.968 | 2.912 | 1.992 |
Specific gravity@15.6 °C | D1298 | 0.828 | 0.800 | 0.716 | 0.798 | 0.792 | 0.790 |
Density@15.6 °C (kg m−3) | D1298 | 827.19 | 799.21 | 714.80 | 797.21 | 791.22 | 789.22 |
Flash point (°C) | D93 | 78 | 36 | −40 | 30 | 28 | 24 |
Cetane index | D976 | 60.18 | 68.98 | 125 | 69.50 | 71.46 | 71.99 |
Gross calorific value (MJ kg−1) | D240 | 45.39 | 44.98 | 36.37 | 44.48 | 43.66 | 43.05 |
Retention time (min) | Chemical compound | Chemical formula | Area (%) |
---|---|---|---|
4.31 | Pentane, 2,2,4-trimethyl- | C8H18 | 0.94 |
4.39 | Heptane | C7H16 | 0.33 |
5.95 | Nonane | C9H20 | 0.52 |
7.67 | Decane | C10H22 | 1.01 |
7.79 | Toluene | C7H8 | 2.07 |
9.59 | 1-Butanol | C4H10O | 2.28 |
10.12 | Ethylbenzene | C8H10 | 0.57 |
10.35 | Undecane | C11H24 | 1.76 |
10.55 | Benzene, 1,2-dimethyl- | C8H10 | 1.04 |
11.87 | Benzene, 1,4-dimethyl- | C8H10 | 0.45 |
13.50 | Benzene, 1-ethyl-4-methyl- | C9H12 | 0.54 |
13.89 | Dodecane | C12H26 | 2.37 |
14.20 | Mesitylene | C9H12 | 0.36 |
15.56 | Benzene, 1,2,3-trimethyl- | C9H12 | 0.99 |
15.83 | Dodecane, 4,6-dimethyl- | C14H30 | 0.33 |
16.14 | Dodecane, 2-methyl- | C13H28 | 0.33 |
17.97 | Tridecane | C13H28 | 2.63 |
22.25 | Tetradecane | C14H30 | 3.20 |
26.54 | Pentadecane | C15H32 | 3.58 |
27.39 | α-Gurjunene | C15H24 | 13.76 |
29.63 | β-Gurjunene | C15H24 | 5.26 |
30.64 | Hexadecane | C16H34 | 3.64 |
31.57 | Alloaromadendrene | C15H24 | 1.57 |
31.96 | γ-Gurjunene | C15H24 | 1.57 |
34.60 | Heptadecane | C17H36 | 3.73 |
38.40 | Octadecane | C18H38 | 3.22 |
41.72 | Nonadecane | C19H40 | 3.01 |
43.21 | Methyl tetradecanoate | C15H30O2 | 0.50 |
44.04 | Eicosane | C20H42 | 2.72 |
45.82 | Heneicosane | C21H44 | 2.54 |
46.87 | Hexadecanoic acid, methyl ester | C17H34O2 | 9.26 |
47.29 | Docosane | C22H46 | 2.27 |
48.74 | Tricosane | C23H48 | 1.88 |
49.91 | Methyl stearate | C19H38O2 | 1.98 |
50.19 | 11-Octadecenoic acid, methyl ester | C19H36O2 | 8.76 |
50.30 | Tetracosane | C24H50 | 1.69 |
50.80 | Linoleic acid, methyl ester | C19H34O2 | 2.99 |
52.07 | Pentacosane | C25H52 | 1.33 |
54.19 | Hexacosane | C26H54 | 1.07 |
56.78 | Heptacosane | C27H56 | 0.81 |
60.01 | Octacosane | C28H58 | 0.67 |
64.08 | Nonacosane | C29H60 | 0.50 |
Retention time (min) | Chemical compound | Chemical formula | Area (%) |
---|---|---|---|
4.35 | Octane | C8H18 | 0.78 |
4.49 | Cyclohexane, 1,4-dimethyl- | C8H16 | 0.82 |
5.05 | Nonane | C9H20 | 1.67 |
5.58 | Nonane, 4-methyl- | C10H22 | 1.61 |
6.16 | Decane | C10H22 | 3.62 |
8.10 | Undecane | C11H24 | 4.18 |
9.13 | p-Xylene | C8H10 | 0.94 |
9.88 | Trans-2-dodecen-1-ol | C12H24O | 1.09 |
10.93 | Dodecane | C12H26 | 5.99 |
11.62 | Benzene, 1-ethyl-3-methyl- | C9H12 | 0.92 |
13.55 | Benzene, 1,2,3-trimethyl- | C9H12 | 1.62 |
14.50 | Tridecane | C13H28 | 6.39 |
15.56 | Benzene, 1,2,4-trimethyl- | C9H12 | 1.4 |
18.49 | Tetradecane | C14H30 | 6.52 |
20.11 | 1-Tetradecene | C14H28 | 1.57 |
22.55 | Pentadecane | C15H32 | 5.66 |
26.53 | Hexadecane | C16H34 | 5.95 |
30.37 | Heptadecane | C17H36 | 5.69 |
34.05 | Octadecane | C18H38 | 4.3 |
37.55 | Nonadecane | C19H40 | 4.01 |
40.80 | Eicosane | C20H42 | 3.9 |
43.18 | Heneicosane | C21H44 | 3.19 |
44.96 | Hexadecanoic acid, methyl ester | C17H34O2 | 10.11 |
46.43 | Tricosane | C23H48 | 2.36 |
47.79 | Methyl stearate | C19H38O2 | 2.06 |
48.07 | 11-Octadecenoic acid, methyl ester | C19H36O2 | 7.59 |
48.68 | Linoleic acid, methyl ester | C19H34O2 | 2.45 |
49.03 | Pentacosane | C25H52 | 1.19 |
50.44 | Hexacosane | C26H54 | 1.13 |
52.10 | Heptacosane | C27H56 | 0.62 |
53.97 | Octacosane | C28H58 | 0.34 |
56.22 | Nonacosane | C29H60 | 0.33 |
Engine parameters | Specifications |
---|---|
Engine model | 4JA1 |
Engine type | 4-Cylinder, 4-cycle, water cooled, direct injection |
Bore × stroke | 93 mm × 92 mm |
Compression ratio | 18.4 |
Displacement | 2449 cc |
Rated power at 4000 rpm | 64.9 kW |
Maximum torque at 2000 rpm | 171.5 N m |
Fuel system | Pump-line-nozzle injection system |
Injection nozzle opening pressure | 18.1 MPa |
Static fuel injection timing | 14° bTDC |
Parameter | Measuring techniques | Measuring range | Resolution | Accuracy | |
---|---|---|---|---|---|
Testo 350 | NO | Chemiluminescence | 0–4000 ppm | 1 ppm | ±5 < 100 ppm |
NO2 | Chemiluminescence | 0–500 ppm | 0.1 ppm | ±5 < 100 ppm | |
CO | Nondispersive infrared | 0–10000 ppm | 1 ppm | ±10 < 200 ppm | |
HC | Flame ionization detector | 0–40000 ppm | 10 ppm | ±400 ppm |
Source | DF | Adj SS | Adj MS | F-Value | P-Value |
---|---|---|---|---|---|
Model | 14 | 416.668 | 29.762 | 1235.19 | 0.000 |
Linear | 6 | 407.799 | 67.966 | 2820.77 | 0.000 |
Engine load (A) | 4 | 406.912 | 101.728 | 4221.95 | 0.000 |
Percentage of diethyl ether (B) | 2 | 0.887 | 0.444 | 18.41 | 0.000 |
2-Way interactions | 8 | 8.869 | 1.109 | 46.01 | 0.000 |
AB | 8 | 8.869 | 1.109 | 46.01 | 0.000 |
Error | 30 | 0.723 | 0.024 | ||
Total | 44 | 417.391 |
Source | DF | Adj SS | Adj MS | F-Value | P-Value |
---|---|---|---|---|---|
Model | 14 | 31.353 | 2.239 | 61.970 | 0.000 |
Linear | 6 | 30.659 | 5.110 | 141.380 | 0.000 |
Engine load (A) | 4 | 22.447 | 5.612 | 155.270 | 0.000 |
Percentage of diethyl ether (B) | 2 | 8.212 | 4.106 | 113.610 | 0.000 |
2-Way interactions | 8 | 0.695 | 0.087 | 2.400 | 0.039 |
AB | 8 | 0.695 | 0.087 | 2.400 | 0.039 |
Error | 30 | 1.084 | 0.036 | ||
Total | 44 | 32.438 |
The input layer, which constitutes the initial layer of the GRNNs architecture, plays a crucial role in the learning process. Within this layer, the training data set, encompassing both input factors (X) and their corresponding output factors (Y), is processed. In this layer, the data retains its original format, and the number of neurons is determined by the dimensionality or levels of the input factors under consideration. Hidden layer 1, also known as the pattern layer, constitutes the second layer within the GRNNs architecture. This layer serves the purpose of transforming the input factor data. To accomplish this transformation, a Gaussian kernel function, specifically a radial basis function, is employed. The Gaussian kernel function quantifies the distance between input factors based on the Euclidean distance metric. Mathematically, the Gaussian kernel function can be represented by eqn (1), wherein hyperparameters influence the prediction performance of the GRNNs model.
(1) |
Hidden layer 2, referred to as the summation layer, constitutes the third layer within the GRNNs architecture. This layer plays a pivotal role in the GRNNs model, as it utilizes the outcomes obtained from the previous layer for mathematical operations. Within this layer, the neurons can be categorized into two distinct types: numerator neurons (SN) and denominator neurons (SD). The numerator neurons are responsible for summing the results derived from multiplying the transformed input data or weights of the GRNNs from the Pattern layer by the corresponding output data associated with those inputs. This computation can be expressed mathematically through eqn (2). Conversely, the denominator neuron solely performs the summation of the transformed input data or weights of the GRNNs, as depicted by eqn (3). Typically, the summation layer of the GRNNs model consists of one denominator neuron, while the number of numerator neurons is contingent upon the vector of the output factors in the given problem.
(2) |
(3) |
The output layer constitutes the fourth layer within the GRNNs architecture. This layer serves the purpose of transforming the output obtained from the learning process back into the original form of the problem's output. This transformation is accomplished through the relationship between the numerator neurons and the denominator neuron, as expressed by eqn (4).
(4) |
In the process of GRNNs modeling, hyperparameter tuning plays a crucial role in enhancing the prediction performance of the model. Specifically, the focus of hyperparameter tuning in this study was on the smoothing parameter (SM). Generally, the hyperparameter tuning process can be carried out through techniques such as grid search or optimization algorithms. For this study, gradient descent optimization was employed, with the aim of minimizing the average root mean square error. To evaluate the effectiveness of the GRNNs model, which utilized a surrogate model of the multi-objective function, it was imperative to determine whether the model exhibited behavior that was consistent with the actual results of the problem. Performance evaluation was conducted using various regression metrics,50 including the coefficient of determination (R2) as defined in eqn (5), the root mean square error (RMSE) as defined in eqn (6) (which measures scale-dependent accuracy), and the median absolute percentage error (MdAPE) as defined in eqn (7) (which assesses percentage error-based accuracy). These metrics provide valuable insights into the model's performance in replicating the observed behavior and serve as quantitative indicators of its predictive capability.
(5) |
(6) |
(7) |
(1) The implementation of NSGA-II was started by setting the goals of the optimization process. In this study, according to the characteristics of engine performance and emissions that usually trade-off behavior, the goals were set as maximum brake thermal efficiency, while nitrogen oxides was set as a minimum following eqn (8). To search for the optimal solution, the engine load and percentage of diethyl ether were set with boundaries following the levels used in the experiment, which are shown in eqn (9).
(8) |
(9) |
(2) After the goals and boundaries of optimization were set, the initial parameters of the NSGA-II were set. The initial population and number of generations of NSGA-II were set at 100.
(3) After all parameters were set, the multi-objective optimization via NSGA-II was started. The prediction results of the GRNNs for each population were generated.
(4) According to the prediction results of the above step, the new parent population were found using crowding testing and non-dominated sorting, and the new offspring population created using crossover and mutation.
(5) Following the setting of the new population, steps (3) and (4) of the optimization process were repeated until the maximum generation was reached.
The results of the brake specific fuel consumption (BSFC) variation during engine load testing are displayed in Fig. 7. It can be observed that as the engine load increases, the BSFC decreases for all test fuels, which is attributed to more efficient heat conversion and less heat loss. However, when compared to diesel fuel, both WPO and all blended fuels exhibit higher BSFC. This can be explained by the lower gross calorific values of WPO and DEE compared to diesel fuel, which necessitates the engine injecting more fuel to maintain engine load. In addition, at low engine load, blended fuels have significantly higher BSFC than WPO, primarily due to the lower gross calorific value of DEE. However, as the engine load increases, the addition of DEE does not lead to a significant increase in BSFC. This is likely due to the higher cetane index and lower viscosity of blended fuels, which improve fuel atomization and ignition delay, thereby enhancing the combustion process. Additionally, the presence of oxygen in the fuel molecules of DEE can contribute to better combustion.4,53 Overall, while the increase in the combustion process due to higher cetane index, lower viscosity and higher oxygen content can balance the decrease in combustion due to higher latent heat of vaporization and lower calorific value of DEE, resulting in similar BSFC when blending more DEE at high engine load.
To provide a comprehensive and precise assessment of the engine's energy efficiency, we evaluated the brake specific energy consumption (BSEC) of the test fuels, as illustrated in Fig. 8. BSEC serves as a measure of the engine's energy consumption rate, taking into consideration both the fuel consumption and energy content. This parameter becomes particularly relevant when comparing the engine's performance under different fuel types with varying energy densities. It is evident from the results that as the engine load increases, the BSEC decreases for all test fuels, indicating a reduced energy consumption rate during engine operation. Notably, the trend in BSEC for all test fuels follows a similar pattern to that observed for BSFC, despite the differing energy densities of the test fuels employed in this study. The combustion of WPO displays a higher BSEC compared to that of diesel fuel. The addition of DEE to the blends does not result in a significant increase in BSEC relative to WPO, except under certain engine load operating conditions where the in-cylinder temperature is insufficient to compensate for the drawback of DEE's high heat vaporization. The rationale used to support the evidence for BSFC across all test fuels can be similarly applied to justify the results of BSEC.
Fig. 11 displays the variations in unburned hydrocarbon (HC) emissions observed with increasing engine loads across all test fuels. The primary causes of HC emissions in diesel engines are cold-region flame-quenching operations and poor combustion. HC emissions of all test fuels generally decrease with increasing engine load due to the higher in-cylinder temperature and improved combustion efficiency. An engine fueled with waste plastic oil and its blended fuels exhibits significantly higher levels than that of diesel fuel at 30 and 50 N m engine load. Additionally, HC emissions tend to increase with an increase in diethyl ether concentration due to the lower in-cylinder temperature resulting from the higher heat of vaporization of DEE. At 70 N m engine load, HC emissions from WPO are similar to those of diesel fuel, while blended fuels continue to exhibit the same trend. At 90 and 110 N m engine loads, HC emissions of WPO and blended fuels are almost identical to diesel fuel, potentially due to a more suitable in-cylinder temperature for improved combustion efficiency. Furthermore, the use of DEE15 at 90 and 110 N m engine load results in lower HC emissions compared to diesel fuel, likely due to the higher availability of oxygen, resulting from the high DEE concentration.23 A similar start of combustion between fuels suggests that the oxygen content present in fuel molecules may contribute to improved combustion. These results suggest that the reduction of HC emissions can be achieved by considering high DEE concentration and high engine load, resulting in the benefits of decreasing HC emissions.
Fig. 12 illustrates the variations in CO emissions observed with increasing engine loads across all test fuels. CO emissions are byproducts of incomplete combustion. CO emissions of all test fuels tend to decrease with increasing engine load, due to higher in-cylinder temperature and improved combustion efficiency. Waste plastic oil (WPO) exhibits higher CO emissions than diesel fuel for all engine loads, which may be due to the higher long-chain hydrocarbon content in WPO, requiring a longer combustion period to achieve complete combustion. Additionally, an increase in diethyl ether (DEE) concentration in blended fuels for 30, 50 and 70 N m engine load results in higher CO emissions than diesel fuel, due to lower in-cylinder temperature, resulting in incomplete combustion. The increase in DEE concentration tends to promote higher CO emissions. The higher latent heat of vaporization and lower gross calorific value with increasing DEE concentration can be used to justify such an increase in CO emissions.6 However, the difference in CO emissions obtained with the combustion of DEE blends compared to WPO is smaller when the engine is operated at high load (90 and 110 N m), where the in-cylinder temperature is high enough to compensate for the effect of the high latent heat of vaporization of DEE. At high engine load a shorter ignition delay, better fuel atomization and higher availability of oxygen content can contribute to improved combustion under the addition of DEE to WPO, resulting in similar CO emissions between fuel blends and WPO, despite increasing DEE concentration. CO emissions are identical for fuel blends and WPO when the engine is operated at 90 N m.
Carbon dioxide (CO2) is a key indicator of complete hydrocarbon fuel combustion. Fig. 13 displays the variation in CO2 emissions with increasing engine loads for all test fuels. CO2 emissions per unit of engine power tend to decrease with increasing engine load. The improvement in combustion process with higher BTE can contribute to the reduction of CO2 emissions when the engine is operated at higher engine load. It is important to note that an increase in CO2 emissions can be observed as engine load increases, when CO2 emissions are expressed as a percentage. When compared with diesel fuel, WPO and its blends tend to have lower CO2 emissions at low engine load, except for DEE15. However, CO2 emissions become similar for all test fuels at high engine load. It should also be noted that DEE blends, with lower calorific value and requiring more fuel to maintain the same engine load, may promote higher CO emissions compared to WPO, even if their contributions to CO2 emissions are similar.
Fig. 14 Results of multi-objective function surrogated by GRNNs model (goal of the optimization). (a) Brake thermal efficiency (%). (b) Nitrogen oxides (g kW−1 h−1). |
The NSGA-II multi-objective optimization, utilizing the GRNNs model as a surrogate for the multi-objective function, yielded optimal results in the form of a Pareto frontier, as depicted in Fig. 16. The Pareto frontier serves as a boundary delineating the trade-off behavior between oil-to-engine performance and emissions, specifically aiming for maximum BTE and NOx. The upper region of the frontier line represents suboptimal outcomes, while the lower region denotes the optimal results. Although the evaluation of optimality based on the Pareto frontier graph is relatively straightforward, translating these results into practical implementation poses challenges. The graph solely provides the line of optimal output factors without explicitly indicating the corresponding input factors or solutions. To facilitate the implementation of the results obtained through NSGA-II optimization, the optimal solutions responsible for the optimal outcomes on the Pareto frontier have been presented in both graphical and tabular forms, as illustrated in Table 8. The analysis of the optimal solutions reveals that the optimal percentage of diethyl ether falls within the range of approximately 10% to 14%. On the other hand, the optimal engine load exhibits a more dispersed distribution, spanning around 30, 40 and 100 N m. These findings shed light on the specific input factors that drive the achievement of optimal outcomes in terms of both oil-to-engine performance and emissions, supplementing the information conveyed by the Pareto frontier graph.
Engine load (N m) | Percentage of diethyl ether (%) | Brake thermal efficiency (%) | Nitrogen oxides (g kW−1 h−1) |
---|---|---|---|
38.51 | 14.17 | 16.665 | 3.721 |
40.03 | 12.48 | 20.098 | 4.833 |
100.91 | 12.56 | 25.711 | 4.941 |
42.99 | 12.47 | 19.426 | 4.618 |
49.99 | 12.48 | 18.689 | 4.376 |
39.99 | 10.28 | 18.351 | 4.268 |
41.98 | 12.42 | 17.449 | 3.975 |
69.19 | 10.78 | 19.044 | 4.491 |
39.99 | 12.47 | 19.486 | 4.637 |
100.43 | 13.13 | 24.710 | 4.930 |
39.99 | 14.73 | 17.032 | 3.826 |
37.99 | 11.48 | 19.825 | 4.742 |
39.99 | 12.04 | 19.069 | 4.512 |
34.98 | 10.18 | 17.277 | 3.919 |
In our previous study,44 which examined the engine performance and emissions resulting from the blending of waste plastic oil produced through the pyrolysis process, with n-butanol at the same diethyl ether ratios as used in our present study (5%, 10% and 15%), optimal outcomes in terms of maximum BTE and minimum NOx were obtained through the NSGA-II multi-objective optimization. These optimal results are depicted as a Pareto frontier in Fig. 17(a). Upon comparing these optimal results with the findings of our current study (Fig. 17(b)), notable differences emerge. Specifically, with regard to the emissions generated from the blended fuel, it was observed that the addition of diethyl ether yielded more favorable outcomes, characterized by lower emissions. Conversely, when considering engine performance metrics in relation to the blended fuel, n-butanol emerged as the optimal solution. These contrasting results suggest that the choice of blending additive for waste plastic oil should be carefully considered, as it entails a trade-off between achieving optimal emissions or optimizing engine performance. The findings from both studies contribute valuable insights for future research and decision-making in the field of fuel additive for improved engine performance and emissions control.
Fig. 17 Comparison of the optimal results via NSGA-II. (a) Optimal result of waste plastic oil mixed with n-butanol. (b) Optimal result of waste plastic oil mixed with diethyl ether. |
• Engine performance decreased with WPO–DEE blends at low engine loads, but significant improvements were observed at high engine loads, with minimal variation as DEE concentration increased.
• Incorporating DEE led to a shorter ignition delay and an earlier start of combustion. However, increasing DEE concentration did not further advance combustion due to higher latent heat of vaporization and lower calorific value, which offset the benefits of DEE's higher cetane index.
• The addition of DEE significantly reduced NOx emissions across all engine loads, without detrimental effects on HC and CO emissions at high engine loads (90 and 110 N m).
• The non-dominated sorting genetic algorithm II (NSGA-II) with generalized regression neural networks (GRNNs) effectively served as a surrogate multi-objective function for optimization. The GRNNs model demonstrated high performance, achieving strong predictive accuracy for performance and emission metrics.
• The NSGA-II optimization revealed an optimal DEE percentage of approximately 10% to 14% for maximum BTE and minimum NOx, with optimal engine loads distributed around 30, 40, and 100 N m.
In order to mitigate the limitations of using waste plastic pyrolysis oils in diesel engines, careful attention must be given to the wax condition in the waste plastic pyrolysis oil, particularly at room temperature. This is crucial to address potential issues that may arise with the fuel injection system. The optimization of relevant parameters in the pyrolysis process for plastic wastes, such as reaction temperature, residence time, catalyst selection, and post-treatment and refining, is essential to minimize the presence of waxes and enhance the overall quality and stability of waste plastic pyrolysis oils. Considering the significance of these endeavors in enhancing the performance and applicability of waste plastic pyrolysis oils in diesel engines, it is recommended that they can be considered as potential areas for future research and development efforts.
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