Home Physical Sciences Multi-objective statistical optimisation utilising response surface methodology to predict engine performance using biofuels from waste plastic oil in CRDi engines
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Multi-objective statistical optimisation utilising response surface methodology to predict engine performance using biofuels from waste plastic oil in CRDi engines

  • Sumit Kanchan , Manisha Priyadarshini , Prem Kumar , Rajesh Choudhary , Swastik Pradhan EMAIL logo , Rajeev Kumar EMAIL logo , Shubham Sharma EMAIL logo , Fuad A. Awwad EMAIL logo , M. Ijaz Khan and Emad A. A. Ismail
Published/Copyright: July 26, 2024
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Abstract

The current research focuses on the optimisation of common rail direct injection (CRDi) diesel engines for their optimum performance and emission characteristics using the response surface methodology (RSM) technique. The RSM approach is used in this study to reduce the number of experimental tests and costs. In the RSM technique, the three input operational parameters such as injection pressures (30, 35, and 40 MPa), engine loads through indicated mean effective pressure (2.1, 4.15, and 6.2 bar), and varying waste plastic oil (WPO)–diesel fuel blends (5%, 10%, and 15%) are considered to improve the engine output responses like brake thermal efficiency (BTE) and nitrogen oxide (NOx) emissions. The polynomial regression model is developed within the defined input parameter range. The validations and prediction accuracy of the regression model are studied using diagnostic and influence plots such as Box–Cox, Cook’s distance, leverage plot, and difference in fits (DFFITS) analysis, to name a few. After the validations of the model, the prediction values of BTE and NOx are compared with the experimental test results. The effects of input parameters on the BTE and NOx emissions are studied by contour and 3D surface plots. The collective effect of NOx and BTE is analysed through an overlay plot at different one-side intervals. The minor change in the outputs of BTE and NOx emissions is studied by sensitivity analysis. The confirmation of the proposed regression model is done through the multi-variate desirability function approach. The results found that the regression model predicts accurately when compared to the experimental test results. The optimal input parameter after the RSM and desirability approach for maximum BTE and lower NOx is found to be 5% of WPO + diesel fuel blend, 30 MPa injection pressure, and 2.1 bar of engine load. Using these parameter sets, the highest value of BTE and the lowest value of NOx emissions are found to be 32.5605% and 14.8757 ppm, respectively.

Graphical abstract

Abbreviations

4S

four-stroke

AC

air-cooled

ANOVA

analysis of variance

BP

brake power

BSFC

brake-specific fuel consumption

BTDC

before top dead centre

BTE

brake thermal efficiency

CA

crank angle

CDRI

common rail direct injection engine

CI

compression ignition

CO

carbon monoxide

CPCB

Central Pollution Control Board

CR

compression ratio

DFBETAS

difference in betas

DFFITS

difference in fits

DI

direct injection

FTIR

Fourier transform infrared

GCMS

gas chromatography–mass spectrometry

HC

hydrocarbon

HDPE

high-density polyethylene

HRR

heat release rate

ID

ignition delay

IP

injection pressure

IT

injection time

LDPE

low-density polyethylene

MCDM

multi-criteria decision-making

PET

polyethylene terephthalate

PM

particulate matter

PP

peak pressure

PP

polypropylene

PPO

plastic pyrolysed oil

PS

polystyrene

PVC

polyvinyl chloride

SWM

solid waste management

TPA

tonnes per annum

WASPAS

weighted aggregated sum product assessment

WC

water-cooled

WPM

weighted product model

WPO

waste plastic oil

WPO

waste plastic oil

WSM

weighted sum model

1 Introduction

Conventional fossil fuels are diminishing over time, and it is predicted that they will become extinct in the next few years. The increasing number of vehicles on the road and the rising carbon emissions from conventional fuel vehicles make it progressively more important to develop non-renewable fossil fuel alternatives [1]. Considering the present energy-economic environmental needs, all alternative biofuels must be easy to renew, have higher availability, and be environmentally friendly to be effective [2,3,4].

Waste plastic oil (WPO) as an alternative fuel has better performance, combustion, and pollution-depletion properties [3]. With increasing amount of waste plastic pollution in the surroundings, biofuels like WPO have shown promising potential to aim at collectively non-renewable fuel and pollution issues. According to Dogu et al. [5], better waste management and wiser product designs are urgently needed to reduce the on-going marine and land pollution caused by solid plastic waste. Sibao et al. [6] have shed light on a direct method of converting polyolefins into liquid fuels and also proposed that this method can selectively convert the plastics into the desired type of fuel, be it gasoline, diesel, jet fuel, or gasoline range hydrocarbons. However, due to the higher aromatic content in WPO, longer ignition delay, higher cylinder pressure, and heat release rate reduce the engine performance and increase the emission of nitrogen oxides (NOx) and other pollutants. The prepared pyrolytic liquid fuel is employed in compression ignition (CI) engines to reduce the use of the conventional fossil fuel, diesel. Table 1 summarises the studies conducted recently on the use of WPO in CI engines as a fuel. As depicted from Table 1, the lower proportion of WPO in the diesel resulted in the increment in the brake thermal efficiency (BTE), while a reduction is reported in the brake-specific fuel consumption (BSFC). Concurrently, a mixed performance in engine emissions like HC, NOx, CO, and CO2 is found.

Table 1

Summary of the collective literature available on WPO and its blend as the engine fuel on the engine performance and emission characteristics

Performance Emission
Reference Diesel % Blend additive WPO % BTE BSFC EGT HC NOx CO CO2
Type %
Devraj et al. [8] 0 DEE 0 100
0 DEE 05 95
0 DEE 10 90
Kaimal and Vijayabalan [9] 0 DEE 0 100
0 DEE 05 95
0 DEE 10 90
0 DEE 15 85
Damodaran et al. [10] 50 n-Butanol 10 40
50 n-Butanol 20 30
50 n-Butanol 30 20
0 n-Butanol 0 100
Damodaran et al. [3] 0 n-Hexanol 30 70
0 n-Octanol 30 70
0 n-Pentanol 30 70
Das et al. [7] 80 Ethanol 10 0
70 Ethanol 15 0
60 Ethanol 20 0
Dillikanan et al. [11] 0 n-Hexanol 0 100
50 n-Hexanol 10 40
50 n-Hexanol 20 30
50 n-Hexanol 30 20
Venkatasan et al. [12] 0 n-Hexanol 0 100
50 n-Hexanol 20 30
50 n-Hexanol 30 20
50 n-Hexanol 40 10
Kaewbuddee et al. [13] 0 0 100
0 Castor oil methyl esters 10 90
0 Palm oil methyl esters 10 90
Syamsiro et al. [14] 80 20
60 Ethanol 20 20
80 100 g Natural gas 20

It is known that testing any alternative fuel is a time-consuming and high-priced practice that involves establishing the results of many operational facets such as fuel injection pressure, fuel injection timing, compression ratio, and load. Therefore, a scientific investigation that comprises the design of the experiment, analysis of variance (ANOVA), establishment of a relation function, and arrangement of findings in the method of surface illustrations is widely explored and adopted. Various optimisation techniques [15,16] to achieve higher thermal efficiencies and emissions within permissible limits have been applied by many researchers. Using scrap plastic chairs to optimise the engine behaviour can have a number of important and pertinent consequences for sustainability and environmental issues. The following are some important things to think about – garbage reduction: one way to lessen the quantity of plastic garbage that clogs landfills and contaminates the environment is to use used plastic chairs as a fuel for engines. Addressing the issue of plastic trash globally is imperative, as it has dire ecological and environmental ramifications. Resource conservation: we can lessen the need for virgin fossil fuels and other resources that are normally needed to power motors by recycling discarded plastic chairs. This can lessen the negative effects that resource extraction has on the environment and aid in the conservation of natural resources. Reduce carbon emissions: plastic chairs can release greenhouse gases and other pollutants when they are burned or turned into fuel. In contrast to conventional fossil fuels, this process may produce less net carbon emissions if it is optimised and the emissions are well managed. A more effective and clean burning process might result from proper optimisation. Energy recovery: by converting used plastic chairs into fuel, it is possible to recover energy that would otherwise be thrown away. This energy can be used to generate electricity, heat buildings, or run automobiles, among other things, promoting sustainability and energy recovery. Circular economy: recycling waste plastic chairs for engine optimisation is in line with the circular economy’s tenets, which emphasise resource reuse, repurposing, and recycling in order to reduce waste and increase the material lifespan. Innovation and research: the use of waste plastics to optimise engine behaviour can spur innovation and research in materials science and sustainable technologies. Innovations in environmental science and engineering may result from finding more effective and sustainable methods to use plastics. Local economic opportunities: by gathering, processing, and using waste plastics for engine optimisation, small-scale businesses and jobs can be established locally, supporting sustainability and economic growth. Regulatory compliance: requirements and rewards may exist in some areas to promote recycling and appropriate plastic disposal. Employing waste plastics to optimise engine behaviour can assist firms in adhering to these laws and even obtaining tax benefits or incentives. Education and public awareness: these programmes can educate the public about the harm that plastic trash does to the environment and the significance of proper waste disposal. Additionally, it can inform individuals of the possible advantages of recycling and reusing plastics. Potential difficulties: when employing waste plastics for engines, it is vital to keep in mind that there can be difficulties with material selection, technological optimisation, and emission management. Effective solutions to these problems will need careful thought and investigation. In conclusion, utilising discarded plastic chairs to optimise engine behaviour can support a circular economy, reduced waste, resource conservation, decreased carbon emissions, and energy recovery. To optimise its advantages and minimise its disadvantages, it must be carried out with an emphasis on environmental responsibility and the development of an effective, sustainable technology. Optimisation tools like response surface methodology (RSM), Taguchi methods, and non-linear regression are largely adopted by various researchers for the performance optimisation of engines. Among these, RSM has emerged as a promising optimisation tool. RSM is very useful for optimising complicated systems with a lot of moving parts and parameters like engine performance, combustion processes, and fuel mixtures. The design of experiments (DOE) is the first step in RSM data collection. When it comes to fuel optimisation, this could entail adjusting a number of variables, including the temperature, air–fuel ratio, ignition timing, and fuel composition, and measuring the effects on emissions and fuel efficiency. The response variables which can be optimised could include engine performance (horsepower, torque), emissions (CO2, NOx, particulate matter), and fuel efficiency (miles per gallon or kilometres per litre). RSM approaches aid in the optimisation of fuel blends for various fuels, including diesel, gasoline, and ethanol, in order to reduce emissions and increase the efficiency. In order to optimise the fuel efficiency and reduce emissions, engines’ air–fuel ratio, injection timing, and compression ratio can also be used in the combustion process. Additionally, it assists in reducing the emissions of pollutants, including particulate matter and NOx. Through the identification of optimal combinations and operating circumstances, this optimisation technique also plays a vital role in the development and optimisation of alternative fuels, such as hydrogen or biofuels.

An instance of an experimental design that makes use of RSM is the Box–Behnken design (BBD). It is especially valuable for processes like fuel optimisation that have several independent variables to optimise. When there are many factors or when doing multiple trials would be costly and time-consuming, it may not be feasible to fully explore all factor combinations. In these cases, the central and factorial point design can be especially helpful. It offers a methodical and effective way to maximise fuel compositions and combustion processes with the least number of required trials.

As an aspect of the RSM technique, the BBD is utilised to reduce the number of experimental trials along with costs.

The BBD is selected due to its ability to identify the implications of input operational parameters on output responses while generating the minimum number of experimental cycles possible. Injection pressures, engine loading as measured by indicated mean effective pressure (IMEP), and varying WPO–diesel fuel blends are the three input parameters considered in the study. BTE and NOx emissions comprise the output responses. When developing, validating, and analysing the polynomial regression model, numerous diagnostic and influence plots are employed.

Identifying and range estimation of input operational parameters and output responses; development of a polynomial regression model utilising reduced ANOVA; confirmation studies utilising a variety of graphs and analyses; and an authentication phase comprising the four stages of the work methodology.

Fifteen different sets or groups of experiments have been generated employing the BBD to generate an experimental matrix with three input parameters and two output responses. Subsequently, statistical analyses, such as ANOVA, are employed in the study to ascertain which process parameters have a substantial impact on the output responses, namely BTE and NOx emissions.

Established advantages like reduced number of experiments, time utilised for mathematical modelling, and cost make it a favourable optimisation tool to achieve better engine performance and lower emissions. Said et al. [17] applied the RSM and BBD-based quadratic models to reduce the number of experiments for conducting the tests on the diesel engine. The study aims to improve the effect of operational parameters like the engine load and injection time on combustion and emission characteristics. The results revealed that the experimental findings are within 7% of the model-predicted output. Bora et al. [18] used RSM for model prediction on a dual-fuel engine. The tests established that the projected outcome is within the 6% error range. Similar experiments are conducted by Vali et al. [19] as they used waste cooking oil for biodiesel production. They recommended that RSM could be an effective way of attaining the finest engine performance and emissions at different operational conditions. Engine parameters such as injection timing, load, fuel flow rate, and blend ratio are adjusted by Singh et al. [20] using RSM through a series of experiments using Pongamia biodiesel to improve the engine behaviour. An investigation by Sakhtivel et al. [21] on a CI engine using a Calophyllum inophyllum bio-diesel fuel blend showed how effectively the RSM technique could be used. They suggested that the RSM-based model could achieve up to 99% accuracy response in contrast to test values. Similarly, in another experiment on WPO, Das et al. [22] used ethanol as an additive along with a diesel blend. They reported higher engine efficiency and reduced emission at a low compression ratio of 18 (18).

From the comprehensive literature available, it is found that exhaustive work is being done in CI engines using WPO to attain the finest engine behaviour by utilising many techniques. But barely any research article is found which uses WPO extracted from the plastic chairs and the optimisation technique applied. In the literature, papers portray the use of mixed plastic waste for WPO production which yields WPO oil having both high-density polyethylene (HDPE) and low-density polyethylene (LDPE) plastics. The current work only focuses on using plastic chairs which comprise only HDPE plastic. Further, limited articles are found on optimising engine behaviour using the collective impact of the injection pressure, load, and fuel blend either through experimentation or by an RSM-based approach. Also, a few papers portray the sensitivity analysis for achieving high BTE and lower engine emission. Therefore, with these literature gaps, the current work is focused on optimising the three operational parameters such as injection pressure, load, and WPO–diesel blends to attain improved BTE and emission, primarily NOx using the RSM. With the WPO fuel prepared from an HDPE source, sensitivity analysis has been conducted to highlight and validate the consequence of each parameter on engine BTE and NOx behaviour, which is also infrequent. To aid in the development of regression models, the data transformation is required to line up the residuals which are projected using the Box–Cox plot [28]. Thereafter, attempts have been made to develop a regression model for the output responses, and the validation of the model is done by comparing it with test values, so that in the future the model can be utilised for finding other test values at different operational parameters without performing the expensive engine tests. With the model developed, the investigation is carried forward to measure how much the regression function changes if some input operational parameter is not included in the model, by using Cook’s distance. Additionally, the analysis is done on how each operational parameter influenced the model fit through leverage plots. Difference in fits (DFFITS) analysis is further used to measure how much the prediction changes if some operational parameter is not included in the model fit. As a final consideration, the difference in betas (DFBETAS) analysis performed for measuring the coefficient measurement changes in cases where a parameter operating in the operational environment is not considered in the model fit, which is rare. The diagnostic approach and a brief role of each tool used in the current study are summarised in Figure 1.

Figure 1 
               Confined summary of the diagnostic process used in Design-Expert software.
Figure 1

Confined summary of the diagnostic process used in Design-Expert software.

2 Research objectives of the current work

Based on the literature review and identifying the research gaps, the present study focuses on achieving the following objectives:

  1. To study the effect of operational parameters such as engine load, injection pressure, and fuel blends to attain optimal engine behaviour through contours and 3D surface plots.

  2. To investigate the optimal operational parameter for improved output response of BTE and NOx using the RSM approach.

  3. To develop a regression model for the output responses, so that it could be utilised for finding test values without performing time-utilising and high-priced tests.

  4. Using statistical approaches such as Box–Cox plots, Cook’s distance, leverage plots, and DFFITS and DFBETAS analyses to analyse the influence of input operational parameters on model fit.

  5. To know the best optimum parameter using desirability analysis.

  6. The sensitivity analysis is carried out to know the effect of the minor change in the important values of the outputs BTE and NOx emission on the optimal value of operational parameters.

3 Fuel preparation and experimental setup

3.1 Collection and preparation of WPO

Waste plastic is retained as the primary source of oil. The composition of the WPO is mainly kept to be plastic chairs, and the collection is from discarded items on the university campus, so they are all nearly identical. A plastic chair can be made of many materials, but most commonly it is made up of HDPE. The waste plastic is pyrolysed in a gaseous fuel heated, batch pyrolysis unit with a handling capacity of 2 kg waste for the production of pyrolytic WPO. The process temperature is kept at 450°C in isothermal conditions for 30 min with a heating rate of 20°C·min−1 from room temperature. The plant for the production of pyrolytic WPO comprises the reactor assembly, condensing unit, separator, and gas collection system. The thermophysical properties of the derived WPO and those of diesel are compared in Table 2.

Table 2

Thermophysical properties of the diesel and WPO fuel

Properties Testing method WPO Diesel
Density @ 15°C (kg/m3) ASTM D1298 799.9 833
Lower calorific value (MJ/kg) ASTM D420 41,323 42,800
Kinematic viscosity @40°C (cSt) ASTM D445 0.75 0.8
Flashpoint (°C) ASTM D93 24 64
Fire point (°C) ASTM D92 34 73

3.2 Engine setup and accompanying accessories

The tests are conducted on a single-cylinder common rail direct injection (CRDi) diesel engine. The schematic diagram of the experimental setup used for the analysis is shown in Figure 2. The engine specifications are listed in Table 3.

Figure 2 
                  Schematic layout of the experimental setup.
Figure 2

Schematic layout of the experimental setup.

Table 3

Engine specifications

Brand Kirloskar
Model TV1 (modified from DI to CRDi)
No. of cylinders and stroke 1, 4
Displacement volume 661 cc
Rated power 5.2 kW
Bore diameter 87.5 mm
Stroke length 110 mm
Compression ratio 17.5:1

The experimental setup is used without any modification (originally converted from DI to CRDi) to employ the WPO-diesel blends. Before starting with the experimental test for the study, the engine is run on a default map using diesel (in CRDi mode) to optimise the indicated thermal efficiency. The engine load is indicated by brake mean effective pressure and is varied from 2.1, 4.15, and 6.2 bar at a constant speed, i.e. at 1,500 rpm. The injection pressure is varied in the range of 30, 35, and 40 deg BTDC. The fuel flow is measured by using a flow meter. AVL Digas-444 is used for measuring emissions. Thereafter, findings are noted for engine combustion, performance, and emission characteristics. For avoiding cyclic variations, an average of 50 cycles is taken during the analysis. The data are recorded three times and are averaged before being reported and analysed. To be certain about the accuracy of the equipment, they are calibrated and tested before conducting the experiments. For independent parameters, the average of data points is taken, and statistical analyses [27] are performed by calculating the mean, standard deviation, and standard error for the repetitive set of 50 readings. The maximum value of the standard error for exhaust gas temperature is noted as ±1.1°C.

4 Work methodology and implementation of RSM

4.1 Work methodology of the current work

The important parameters which determine engine performance and emissions are injection strategies, varying fuel blends, and engine load. It is pertinent to mention here that this study takes into account only the injection pressure to find its optimal values using a statistical approach, along with optimal varying fuel blend and engine load for enhanced performance and emission output. Furthermore, engine output characteristics such as BTE and NOx are examined for maximising and minimising their values, respectively. The bird eye view engine model of the study depicting the input and output is shown in Figure 3. The permissible range of every input operational parameter is designated by the prior observations based on the rate of pressure rise and stable operation of the preferred engine operation. The range estimation according to prior experimentation of each input operational parameter is shown in Table 4.

Figure 3 
                  Bird’s eye view of the employed engine model with input and output variables.
Figure 3

Bird’s eye view of the employed engine model with input and output variables.

Table 4

Identification of range for input variable parameters

S. No. Variable parameters Units Range of individual variable parameters adopted for design
Minimum Maximum
1 WPO + diesel fuel blend % 5 20
2 Engine load (IMEP) bar 2.1 6.2
3 Injection pressure MPa 30 45

The work methodology adopted for the current work is shown in Figure 4. It can be observed from Figure 4 that the whole methodology is divided into four phases, i.e. first, identification and range estimation of input operational parameters and output responses. Second, the development of a polynomial regression model using reduced ANOVA and its analysis. Third, carrying confirmation studies based on normality plots, leverage plot, contour and 3D surface plots, Box–Cox plot, Cook’s plot, DDFITS analysis, and DFBETAS analysis, and fourth the authentication phase. The current work presents the comprehensive analysis of the experimental design to optimise outcomes in the subsequent sections.

Figure 4 
                  Block diagram of work methodology for multi-parametric optimisation.
Figure 4

Block diagram of work methodology for multi-parametric optimisation.

4.2 RSM setup

RSM is used to model and analyse a process using mathematical and statistical models in which the response is affected by process variables [23]. This technique aids in developing a correlation between the input operational parameters and the output responses. Using this technique, the influence, level of influence, and depth of interaction between the input and output responses are determined, by implying the Box–Cox plot, Cook’s distance, contour and 3D surface plots, and DFFITS and DFBETAS analyses. In the current study, the effect of input operational parameters, such as injection pressure, load, and WPO + blends, on output parameters, such as BTE and NOx, is determined for WPO-fuelled CRDi diesel engines. This process helps in the optimisation of the engineering process to obtain an optimum response with multiple variables that significantly influence the response. Any output parameter that gives an idea of the quality of the process is known as a response, and the RSM outlines a functional relation between the input variables and the output responses, as given in Eq. 1, where ε stands for noise and error, and f represents the second-order polynomial function with independent variables, Eq. 2,

(1) y = f ( x 1 , x 2 , x 3 , x 4 ,   x 5 ) ± ε

(2) f ( x ) = β 0 + i = 1 k β i x i +   i = 1 k β i i x i 2 + i k i k β i j x i x j   +   ε

where β 0 , β i , β i i , and j are coefficients of the regression model.

The response data are used in the equations to find out the RSM model regression coefficient. ANOVA is carried out to know the influential process parameters for the output responses. The RSM is designed as per the BBD so that a minimum number of experimental runs can be generated as compared to other design methods. Further, the R-squared value and the adjusted and predicted R-squared values are noted for validation of the regression equation.

4.2.1 BBD for multivariate optimisation

In an exhaustive study done by Ferreira et al. [29], they discussed the fundamentals, advantages, and limitations of the BBD. In the current work, BBD is used to design the experimental matrix, where three input operational parameters show interaction with two output responses to obtain 15 sets of experiments. The goal, weights, and importance for each adopted parameter are tabulated as shown in Table 5.

Table 5

Goal, weights, and importance of each selected input and output parameters

Name Goal Lower limit Upper limit Lower weight Upper weight Importance
A: fuel blend is in range 5 15 1 1 3
B: injection pressure is in range 30 40 1 1 3
C: load (IMEP) is in range 2.1 6.2 1 1 3
BTE maximise 10.5 32.5 1 1 3
NOx minimise 23 268 1 1 3

The number of experiments (N) required for the development of BBD can be simply written as Eq. 3:

(3) N = 2 k   ( k 1 ) +   C O

where k is the number of factors and C O is the number of central points.

Thus, with the given formula and the underlying theory that BBD designs always have three levels for each parameter to fit a polynomial model for three input operational parameters and two output responses, and we realised 15 experimental runs. The input operational parameters taken are injection pressure, load and fuel blends, and the output responses taken are BTE and NOx emission. The experimental matrix with coded and non-coded forms developed using the BBD under the RSM technique is displayed in Table 6.

Table 6

Experimental layout as per the BBD with output responses

Fuel blend Injection pressure Load (IMEP) BTE NOx emission
Units % MPa Bar % ppm
1 5 30 4.15 17.2 165
2 5 35 2.1 30.5 34
3 5 35 6.2 11.5 255
4 5 40 4.15 15.3 230
5 10 30 2.1 32.4 43
6 10 30 6.2 12.5 205
7 10 35 4.15 14.1 250
8 10 35 4.15 14.2 240
9 10 35 4.15 14.2 245
10 10 40 2.1 30.7 23
11 10 40 6.2 10.5 268
12 15 30 4.15 16.1 180
13 15 35 2.1 32.5 92
14 15 35 6.2 11.2 236
15 15 40 4.15 16.3 230

5 Results and discussion

The results obtained from the experiments performed are provided in the following sections where the impact and assessment analysis of the input operational parameters on the output responses is done by dividing the analysis into two categories. First, after developing a reduced ANOVA table, diagnostics plots are drawn for BTE and NOx. Second, an influence plot is drawn to find the significant parameter affecting the output response. Thereafter, the desirability and sensitivity analysis is carried out to know the depth of influence of input parameters over the output responses. Moreover, a comparison between the experimental value and the predicted value of the regression model for the output response is done and percentage change is noted.

5.1 Statistical response analysis

5.1.1 ANOVA

Design-Expert v12 is used for the current study. The ANOVA test is carried out to know the significant process parameters influencing the output responses. The ANOVA table of BTE is shown in Table 7. From the ANOVA table, the insignificant interaction term is removed and a new reduced ANOVA test is done. So, the accuracy of the prediction data will be increased than that obtained from the regression equation model of BTE [30].

Table 7

ANOVA for BTE

Source Sum of squares Df Mean square F-value p-value
Model 962.10 9 106.90 583.09 <0.0001
A – fuel blend 0.3200 1 0.3200 1.75 0.2437
B – injection pressure 3.64 1 3.64 19.88 0.0066
C – load 808.02 1 808.02 4407.38 <0.0001
AB 1.10 1 1.10 6.01 0.0578
AC 1.32 1 1.32 7.21 0.0435
BC 0.0225 1 0.0225 0.1227 0.7404
A² 3.54 1 3.54 19.31 0.0071
B² 4.30 1 4.30 23.45 0.0047
C² 145.58 1 145.58 794.07 <0.0001
Residual 0.9167 5 0.1833
Lack of fit 0.9100 3 0.3033 91.00 0.0109
Pure error 0.0067 2 0.0033
Cor total 963.02 14

From Table 7, it can be observed that the model F value is 583.09, which states that the model is significant. The predicted R² of 0.9849 is in reasonable agreement with the adjusted R² of 0.9973. P-values less than 0.0500 indicates that model terms are significant. In this case, B, C, AC, A², B², and C² are significant model terms. Since the process parameter cannot be removed, the reduced ANOVA is formed by removing the interaction term BC, as shown in Table 8.

Table 8

Reduced ANOVA for BTE

Source Sum of squares Df Mean square F-value p-value
Model 962.08 8 120.26 768.30 <0.0001
A – fuel blend 0.3200 1 0.3200 2.04 0.2027
B – injection Pressure 3.64 1 3.64 23.29 0.0029
C – load 808.02 1 808.02 5162.15 <0.0001
AB 1.10 1 1.10 7.04 0.0378
AC 1.32 1 1.32 8.45 0.0271
A² 3.54 1 3.54 22.62 0.0031
B² 4.30 1 4.30 27.47 0.0019
C² 145.58 1 145.58 930.06 <0.0001
Residual 0.9392 6 0.1565
Lack of fit 0.9325 4 0.2331 69.94 0.0141
Pure error 0.0067 2 0.0033
Cor total 963.02 14

From the reduced ANOVA table, Table 8, it can be observed that the model F-value increases to 768.30, which implies the model is more accurate. The value of predicted R² increases to 0.9879 and the adjusted R² increases to 0.9977. Hence, this ANOVA model can be considered for further analysis. Engine load is the most significant parameter that influences the BTE, followed by injection pressure and WPO + diesel fuel blend with p-values of 0.0001, 0.0029, and 0.2027, respectively. Similarly, the ANOVA test is done for NOx emission, as shown in Table 9.

Table 9

ANOVA for the NOx emission

Source Sum of squares Df Mean square F-value p-value
Model 1.066 × 105 9 11,840.71 59.77 0.0001
A – fuel blend 364.50 1 364.50 1.84 0.2330
B – injection pressure 3,120.50 1 3,120.50 15.75 0.0106
C – load 74,498.00 1 74,498.00 376.06 <0.0001
AB 56.25 1 56.25 0.2839 0.6169
AC 1,482.25 1 1,482.25 7.48 0.0410
BC 1,722.25 1 1,722.25 8.69 0.0319
A² 542.83 1 542.83 2.74 0.1588
B² 3,692.83 1 3,692.83 18.64 0.0076
C² 22,825.44 1 22,825.44 115.22 0.0001
Residual 990.50 5 198.10
Lack of fit 940.50 3 313.50 12.54 0.0748
Pure error 50.00 2 25.00
Cor total 1.076 × 105 14

From the ANOVA table, Table 9, it can be observed that the model F-value of 59.77 recommends that the model is significant. P-values less than 0.0500 indicate that model terms of NOx emission are significant. In this case, B, C, AC, BC, B², and C² are significant model terms. The predicted R² of 0.8590 is in reasonable agreement with the adjusted R² of 0.9742. Since the process parameter cannot be removed, the reduced ANOVA is formed by removing the interaction term AB and A², as shown in Table 10.

Table 10

Reduced ANOVA table of NOx emission

Source Sum of squares Df Mean square F-value p-value
Model 1.060 ×105 7 15,138.19 66.66 <0.0001
A – fuel blend 364.50 1 364.50 1.61 0.2457
B – injection pressure 3,120.50 1 3,120.50 13.74 0.0076
C – load 74,498.00 1 74,498.00 328.07 <0.0001
AC 1,482.25 1 1,482.25 6.53 0.0378
BC 1,722.25 1 1,722.25 7.58 0.0283
B² 3,498.92 1 3,498.92 15.41 0.0057
C² 22,419.78 1 22,419.78 98.73 <0.0001
Residual 1,589.58 7 227.08
Lack of fit 1,539.58 5 307.92 12.32 0.0768
Pure error 50.00 2 25.00
Cor total 1.076 × 105 14

From the reduced ANOVA table, Table 10, it can be observed that the model F-value increases to 66.66. The predicted R² increases to 0.8988 and is in reasonable agreement with the adjusted R² of 0.9704. It is observed that engine load is the most significant parameter that influences NOx emission, followed by injection pressure and WPO + diesel fuel blend with p-values of 0.0001, 0.0076, and 0.2457, respectively [30,31].

5.2 Diagnostic plot of the model for BTE and NOx

It is pertinent to mention here that authors have divided the statistical response analysis into two phases, i.e. diagnostic and influence plots. Investigative analysis of the model prepared is done to validate whether the proposed model will be accurate or not.

5.2.1 Surface plots, contours, interactions, and residuals have the following implications

It is essential to include succinct explanations regarding the consequences of contours, interactions, residuals, and surface plots. The visualisations function in multiple manners to aid in the confirmation and comprehension of the regression model [32,33].

5.2.2 Surface contours and 3D plots

The interaction effects among various input parameters and the output responses (BTE and NOx) are graphically depicted in these plots.

Implications: Define regions of optimum performance and emissions, demonstrating the influence of operational parameter variations on the engine’s behaviour.

5.2.3 Plots of residuals versus expected

By examining the residual distribution, these graphs aid in evaluating the statistical validity and mathematical reliability of the regression model.

Implications: The presence of a consistent pattern in residuals serves as an indicator of the accuracy of the model, whereas anomalies may indicate potential areas that require refinement of the model.

5.2.4 Plots of normal probability

By examining the residuals for normality, these graphs verify that the model’s assumptions are satisfied.

Implications: The reliability of the model is indicated by a linear distribution along the expected line.

5.2.5 Prediction and validation accuracy

It is vital to discuss the methods utilised for validation, including diagnostic and influence diagrams in the regression model, such as Box–Cox, Cook’s distance, leverage, and DFFITS, which enhance its credibility.

5.2.6 Normal probability and residuals versus predicted

Elucidate how validating the randomness and normality of residuals through these plots ensures the accuracy of predictions.

Compare the Run Plot with Residuals Plot and explain how the latter aids in the detection of unknown variables and assures the experiment’s stability.

5.2.7 Plots predicted versus actual

Explore on the agreement between anticipated predicted and observed values, underscoring the reliability of the model.

5.2.8 Box–Cox analysis of plots

The Box–Cox plots’ role in determining the necessity for power transformations will be examined. The absence of any transformation indicates that the model is robust.

5.3 Implications of residuals versus expected plots and normal probability plots

5.3.1 Plots for normal probability

Normal probability graphs are valuable plots for determining whether residuals follow a normal distribution. The presence of a linear distribution accompanied by minimal fluctuations offers assurance regarding the accuracy of the model’s predictions. The lack of substantial deviations from the mean value indicates that the model’s assumptions are valid, thereby strengthening the reliability of the predictions.

5.3.2 Plots of residuals versus expected

Plots for residuals versus expected validate the regression model. The absence of a discernible pattern in the random distribution of points indicates that the model is adequate. The lack of discernible patterns indicates that the output response is not being influenced by unknown variables, which provides additional evidence for the regression model’s accuracy.

5.3.2.1 Normal probability

The normality plots of residuals for the BTE and NOx emission are shown in Figure 5a and b, respectively. It can be seen that the error value and the residual value are distributed along a linear line with a small fluctuation in both cases, which indicate the model predictions will give an accurate result.

Figure 5 
                        (a) Normal probability residual plot of BTE. (b) Normal probability residual plot of NOx emission.
Figure 5

(a) Normal probability residual plot of BTE. (b) Normal probability residual plot of NOx emission.

5.3.2.2 Residuals vs predicted

The residuals versus predicted plots are shown in Figure 6a and b for BTE and NOx emissions, respectively. It can be visualised from these plots that the model created till now is satisfactory and can be further used to generate the regression equations. No specific pattern is observed in these plots as the points are randomly distributed, which signifies the accuracy of the proposed regression model. This is observed for both BTE and NOx emissions.

Figure 6 
                        (a) Residuals versus predicted plot of BTE. (b) Residuals versus predicted plot of NOx emission.
Figure 6

(a) Residuals versus predicted plot of BTE. (b) Residuals versus predicted plot of NOx emission.

5.3.2.3 Residuals vs run plot

The residuals versus run plots for BTE and NOx are plotted in Figure 7a and b, respectively. These plots help to check the unknown and not controlled variable or lurking variable that influences the output response during the experiment. A trend in the plot time-related variable is present in the background. A random scatter plot is observed, which indicates that no lurking variables are present in the experiment. The residual versus run plot of BTE varies the internally studentized residuals from −2.401 to 2.401. Similarly, the NOx emission varies the internally studentized residuals from −1.656 to 2.374.

Figure 7 
                        (a) Residual versus run plot of BTE. (b) Residual versus run plot of NOx emission.
Figure 7

(a) Residual versus run plot of BTE. (b) Residual versus run plot of NOx emission.

5.3.2.4 Predicted vs actual plots

The predicted versus actual plots for BTE and NOx emission are shown in Figure 8a and b, respectively. The plots show an agreement of the actual values with the predicted value of the proposed regression model. It can be observed that the BTE and NOx emission data are approximately normally distributed along the linear line with minor fluctuations (especially in the case of NOx).

Figure 8 
                        (a) Predicted versus actual values of BTE. (b) Predicted versus actual values of NOx emission.
Figure 8

(a) Predicted versus actual values of BTE. (b) Predicted versus actual values of NOx emission.

5.3.2.5 Box–Cox plot analyses of BTE and NOx

The Box–Cox plot for the power transforms for BTE and NOx emission is plotted in Figure 9a and b, respectively. The Box–Cox plot helps to find out the most suitable power transformation that can be applied to the response data. The power law transformations can be applied to the responses if the value is greater than zero. The transformations lead to improvement in statistical analysis and diagnostic plots of the responses. The power transformation is represented by lambda.

Figure 9 
                        (a) Box–Cox plot for power transforms of BTE. (b) Box–Cox plot for power transforms of NOx emission.
Figure 9

(a) Box–Cox plot for power transforms of BTE. (b) Box–Cox plot for power transforms of NOx emission.

Lambda = 1 indicates no transformation; Lambda = 0.5 indicates the square root; Lambda = 0 indicates the natural log; Lambda = −0.5 indicates the inverse square root; Lambda = −1 indicates inverse.

In this study, the lambda value for BTE is 0.81, and for NOx emission it is 1, including the 95% confidence interval. Since the lambda values of both BTE and NOx emissions are nearly equal to 1, no transformation is suggested.

After analysing the diagnostic plots, the following observations are noticed:

  1. The residuals and predicted vs actual points of the BTE and NOx emissions are aligned along the normalised lines, which indicates that the prediction of the proposed regression model will be more accurate.

  2. It is noticed that the predicted vs residuals are distributed randomly with no lurking variables, which confirms the prediction accuracy of the proposed model [34,35].

  3. No power transform for both BTE and NOx is suggested as the lambda values are near 1.

5.3.3 Influence plots of BTE and NOx

5.3.3.1 Leverage vs run number plots of BTE and NOx

Figure 10a and b shows the leverage versus run plot for BTE and NOx emission, respectively. The leverage plot shows the impact of individual design points on the model’s predicted values. The leverage value of the individual run varies from 0 to 1. The leverage value of 1 signifies that the residuals will be zero. It indicates the predicted value of regression model is equal to the experimental value. An experiment can have a maximum leverage of 1/k, where k is termed as the number of times the experiment is repeated. For calculating the leverage value, Eq. 4 is used.

(4) H = X ( X T X ) 1 X T ;  Leverage  =  diag  ( H )

where H represents the (n × n) symmetric matrix, X is the term used as the model matrix, and T is the transpose. It has one row for every design (n) and one column for every term in the model (p). The leverage represents the diagonal elements of the H matrix. It is observed that the leverage value of BTE lies between 0.333 and 0.75, and the leverage value range for NOx emission lies within the range of 0.231–0.692. This shows that the deviations of the leverage value for BTE and NOx lie within the defined range of 0 to 1 and are inclined towards 1. This implies predictions of the proposed regression model will be accurate for both.

Figure 10 
                        (a) Leverage versus run plot of BTE. (b) Leverage versus run plot of NOx emission.
Figure 10

(a) Leverage versus run plot of BTE. (b) Leverage versus run plot of NOx emission.

5.3.3.2 DDFITS vs run analysis of BTE and NOx

Figure 11a and b shows the DFFITS versus run plot for BTE and NOx emission. The DFFITS value analyses the effect of ith observation on the predicted value. It is calculated as the difference between the predicted value with the observed i and the predicted value without considering i. This is shown in Eq. 5.

(5) Y ˆ ( i ) = Y + e 1 Leverage DFFITS = Y ¯ Y ( i ) ^ ^ σ ˆ ( i ) 2 .  Leverage ^

The range of DFFITS value for most of the BTE responses is –2.33 to 2.33. The range of DFFITS value for most of the NOx emission responses is −2.950 to 3.308.

Figure 11 
                        (a) DFFITS versus run plot of BTE. (b) DFFITS versus run plot of NOx emission.
Figure 11

(a) DFFITS versus run plot of BTE. (b) DFFITS versus run plot of NOx emission.

5.3.3.3 DFBETAS for intercept vs run analysis of BTE and NOx

The DFBETAS plot for the BTE and NOx emission is shown in Figure 12a and b, respectively. It shows the impacts of ith observation on each of the regression coefficients. If the ith observation is removed, then the number of standard order that the jth coefficients vary is termed DFBETAS j,i. This is shown in Eq. 6.

(6) DFBETAS j , ( i ) = β j β j , ( i ) ^ σ ˆ ( i ) , i 2 . ( X T X ) j j 1

A large value of DFBETAS j,i signifies that the ith observation has higher impacts on the jth regression coefficient. From the BTE DFBETAS intercept versus run plot, the range of DFBETAS j,i is found to be −0.13369 to 0.066667, and the NOx emission DFBETAS j,i range is found to be −0.567747 to 0.51179.

Figure 12 
                        (a) DFBETAS versus run plot of BTE. (b) DFBETAS versus run plot of NOx emission.
Figure 12

(a) DFBETAS versus run plot of BTE. (b) DFBETAS versus run plot of NOx emission.

5.3.3.4 Cook’s distance vs run number analysis

Figure 13a and b shows the Cook’s distance with the run number for BTE and NOx. The Cook’s distance measures the variation of the regression model if the ith point will not be considered at the time of fitting the model. Cook’s distance (D i) is calculated by the product of the square of ith internally studentized residual and a monotonic function of the leverage, as shown in Eq. 7.

(7) D i =   r i 2 p + 1 Leverage i 1 Leverage i

It is a standardised weighted distance that is calculated between the vector of regression coefficients found from the test set and the reduced test set compared with the error mean squared of the fitted model. The less the value of the Cook’s distance, the better the fitting of the model is achieved [36,37]. It can be seen that the model fitting is adequate.

Figure 13 
                        (a) Cook’s distance plot of BTE. (b) Cook’s distance plot of NOx emission.
Figure 13

(a) Cook’s distance plot of BTE. (b) Cook’s distance plot of NOx emission.

6 Regression equation

It can be visualised from all obtained diagnostics and influence plots that the model created till now is satisfactory and can be further used to generate the regression equations. The final regression equation for the BTE and NOx emission is generated and mentioned as Eqs 8 and 9.

(8) Brake thermal efficiency = 126.38758 1.24552 Fuel Blend 3.36666 Injection Pressure 16.742910 Load + 0.02100 × Fuel Blend Injection Pressure 0.05609 Fuel Blend × Load + 0.03916 Fuel Blend ² + 0.04316 Injection Pressure ² + 1.49415 Load ² ,

(9) NOx Emission = 1715.77980 + 9.14390 Fuel Blend + 81.48724 Injection Pressure + 148.44346 Load 1.87805 Fuel Blend × Load + 2.02439 Injection Pressure × Load 1.22769 Injection Pressure ² 18.48716 Load ²

These regression equations can be further used to predict the given process parameter and their levels to find out the BTE and NOx emission values at the defined point. Figures 14 and 15 show the actual data versus predicted data from the regression equation of BTE and NOx emission, respectively. It depicts that regression model-predicted data are predicted accurately with average percentage errors of 1.3% and 8.2% when compared with the experimental value of BTE and NOx emission.

Figure 14 
               Comparison of experimental versus predicted values of BTE.
Figure 14

Comparison of experimental versus predicted values of BTE.

Figure 15 
               Comparison of experimental versus predicted values of NOx emission.
Figure 15

Comparison of experimental versus predicted values of NOx emission.

7 Optimisation of the input operational parameters

Figure 16 
               (a) Contour plot for BTE with the fuel blend and injection pressure. (b) 3D surface plot for BTE with fuel blend and injection pressure.
Figure 16

(a) Contour plot for BTE with the fuel blend and injection pressure. (b) 3D surface plot for BTE with fuel blend and injection pressure.

Figure 17 
               (a) Contour plot for BTE with the fuel blend and load. (b) 3D surface plot for BTE with fuel blend and load.
Figure 17

(a) Contour plot for BTE with the fuel blend and load. (b) 3D surface plot for BTE with fuel blend and load.

Figure 18 
               (a) Contour plot for BTE with injection pressure and load. (b) 3D surface plot for BTE with injection pressure and load.
Figure 18

(a) Contour plot for BTE with injection pressure and load. (b) 3D surface plot for BTE with injection pressure and load.

7.1 BTE

Figure 16a and b shows the contour and 3D surface plots for a combined effect of the fuel blend and injection pressure on the BTE. It can be observed that combining both does not significantly affect the change in BTE. Figure 17a and b shows the contour and 3D surface plots for the combined effect of fuel blend and load on the BTE. It can be detected that by increasing the fuel blend percentage and increasing the load value the BTE increases. Figure 18a and b shows the contour and 3D surface plots for the combined effect of injection pressure and load on the BTE. It can be seen that by increasing both the injection pressure and load the BTE increases.

7.2 NOx emission

Figure 19a and b depicts that by increasing the fuel blend percentage and injection pressure the NOx emission will be reduced. The NOx emission will increase if the lower injection pressure is combined with any type of fuel blend percentage considered in this study. From Figure 20a and b, it can be observed that with a low fuel blend percentage and high load value the NOx emission decreases [38]. The NOx emission can be reduced by combinedly increasing the injection pressure and the load value, as shown in Figure 21a and b of contour and 3D surface plots, respectively.

Figure 19 
                  (a) Contour plot for BTE with fuel blend and injection pressure. (b) 3D surface plot for BTE with fuel blend and injection pressure.
Figure 19

(a) Contour plot for BTE with fuel blend and injection pressure. (b) 3D surface plot for BTE with fuel blend and injection pressure.

Figure 20 
                  (a) Contour plot for BTE with fuel blend and load. (b) 3D surface plot for BTE with fuel blend and load.
Figure 20

(a) Contour plot for BTE with fuel blend and load. (b) 3D surface plot for BTE with fuel blend and load.

Figure 21 
                  (a) Contour plot for BTE with injection pressure and load. (b) 3D surface plot for BTE with injection pressure and load.
Figure 21

(a) Contour plot for BTE with injection pressure and load. (b) 3D surface plot for BTE with injection pressure and load.

8 Optimisation of multi-responses by the desirability function approach

Since maximising BTE performance and minimising NOx emission is generally beneficial for engines, the engine's performance through BTE and exhaust emission NOx emissions are two opposing output reactions. Hence, both need to be improved altogether, thus the process parameter needs to be optimised through multiple-response optimisation methods. The respective goal, limits, weights, and importance are listed in Table 5.

The desirability function method is applied in this study to find out the optimal process parameter for higher BTE and lower NOx emissions.

Figures 22 and 23 show the effect of the process parameter and contour plot on the output responses with the desirability approach. In Figure 22, the red cross mark indicates that the BTE will be maximum and NOx will be minimum at lower values of WPO + diesel fuel blend, injection pressure, and engine load. The actual values of the optimised process parameter are found to be 5.46616% for WPO + diesel fuel blend, 30.2124 MPa for injection pressure, and 2.10022 bar for engine load. The same can be observed from the contour plot in Figure 23. In this process parameter setting, the engine performance will be optimised well with the D value of 1, BTE of 32.5605, and NOx emission of 14.8757, as shown in Figure 24.

Figure 22 
               Multi-response optimisation using the desirability function method.
Figure 22

Multi-response optimisation using the desirability function method.

Figure 23 
               Contour plots for the desirability approach of output responses.
Figure 23

Contour plots for the desirability approach of output responses.

Figure 24 
               Optimal process parameter conditions using the desirability approach.
Figure 24

Optimal process parameter conditions using the desirability approach.

8.1 Overlay plots

Figures 25a and 26b show the overlay plot between the BTE and NOx emission at various one-side intervals. The overlay plot shows the critical response contours on a contour plot, so that the common area can be picked as the best solution among all responses. In the overlay plot, grey colour indicates the area that is not fit for the optimisation criteria. The dark gold colour of the overlay plot portrays the area where the point estimate meets the criterion requirements. The bright yellow colour represents the area where the entire range of all intervals meet the specified criteria. The one-side interval estimation can be added to the overlay plot, which helps to comprehend the influence of uncertainty on accomplishing process goals. Three types of one-side interval are considered, and the overlay plots of BTE and NOx emission with the interval of confidence, prediction, and tolerance with an alpha value of 0.05 are plotted as shown in the Figures 25a and 26b. Figure 25b shows the overlay plot of BTE and NOx emission with interval of confidence. The confidence interval of the BTE is consider to be high and that of the NOx emission is considered to be low, and the overlay plot is plotted. In this plot, the bright yellow colour area shows the sweet spot or the area where the entire range of all intervals meet the specified criteria. Figure 26a depicts the overlay plot of BTE and NOx emission with 95% interval of prediction. The BTE prediction interval is considered as high, and the NOx emission prediction interval is considered as low. The bright yellow area in the plot depicts the suitable criteria. Figure 26b portrays the overlay plot of BTE and NOx emission with 0.99 tolerance interval. In this, the dark gold colour area of the plot is the area where the point design estimation meets the requirement criteria.

Figure 25 
                  (a) Overlay plot of BTE and NOx emission. (b) Overlay plot of BTE and NOx emissions with 95% confidence level.
Figure 25

(a) Overlay plot of BTE and NOx emission. (b) Overlay plot of BTE and NOx emissions with 95% confidence level.

Figure 26 
                  (a) Overlay plot of BTE and NOx emissions with 95% prediction level. (b) Overlay plot of BTE and NOx emissions with 0.99 tolerance level.
Figure 26

(a) Overlay plot of BTE and NOx emissions with 95% prediction level. (b) Overlay plot of BTE and NOx emissions with 0.99 tolerance level.

9 Sensitivity analysis

Sensitivity analysis is carried out to know the effect of the minor change in the important values of the outputs BTE and NOx emission on the optimal value of the process parameters and their correlation with distinct uncertainty obtained from the RSM method. This uncertainty has a major influence on the sensitivity of the model outputs. Hence, the sensitivity analysis has to be done to know the sustainability of the regression equation by examining the design functions of the objectives with the process parameter of the design [2426]. The sensitivity analysis is performed for BTE and NOx emission with the three-process parameter, i.e. fuel blend percentage, injection pressure, and load. A total of six sensitivity Eqs. 1015 are found by differentiating the regression equations of BTE and NOx emission.

(10) δ ( η BTE ) / δ Fuel Blend = 1.24553 + 0.021 × Injection Pressure 0.05609 × Load + ( 2 × 0.03916 ) × Fuel Blend

(11) δ ( η BTE ) / δ Injection Pressure = 3.36667 + 0.021 × Fuel Blend + ( 2 × 0.04316 ) × Injection Pressure

(12) δ ( η BTE ) / δ Load = 16.74291 0.05609 × Fuel Blend + ( 2 × 1.49415 ) × Load

(13) δ ( NOx ) / δ Fuel Blend = 9.1439 1.87805 × Load

(14) δ ( NOx ) / δ Injection Pressure = 81.48724 + 2.02439 × Load ( 2 × 1.22769 ) × Injection Pressure

(15) δ ( NOx ) / δ Load = 148.44346 1.87805 × Fuel Blend + 2.02439 × Injection Pressure ( 2 × 18.48716 ) × Load

The sensitivity analysis depicts the best possible engine performance and their uncertainty to any variation made in the defined regression model process parameters of the engine. The sensitivity values of the BTE and NOx emission of the engine are calculated using the process parameter value considered in this study. The injection pressure considered in sensitivity analysis is low, i.e. 30 MPa, and the load is considered to be low and high, i.e. 2.1 and 6.2 bar, respectively, with low medium and high values of fuel blend percentage. The sensitivity values of BTE and NOx emission are graphically plotted in Figures 27 and 28, respectively.

Figure 27 
               Sensitivity analysis for BTE.
Figure 27

Sensitivity analysis for BTE.

Figure 28 
               Sensitivity analysis for NOx emission.
Figure 28

Sensitivity analysis for NOx emission.

From Figure 27, it can be depicted that the sensitivity of BTE with WPO + diesel fuel blend increases as the waste plastic energy share increases. The sensitivity of BTE to the load decreases, with the increase in the WPO + diesel fuel blend. The sensitivity of BTE to the injection pressure increases marginally with an increase of the WPO + diesel fuel blend.

Figure 28 shows the sensitivity analysis for NOx emission. It can be observed that the sensitivity of NOx emission with engine load decreases with increases in the WPO + diesel fuel blend. Further, the sensitivity of NOx emission to the fuel blend and injection pressure remains constant.

10 Conclusions

From the objectives defined, experiments performed, and analysis, as reported in the above sections, the following conclusions could be drawn from the work.

  1. Investigation performed using diagnostic plots revealed that the prediction value from the proposed regression model for BTE and NOx emission could be considered equal to the experimental tests.

  2. Engine load and injection pressure are found to be a significant factor for both BTE and NOx emission.

  3. The order of importance of the input parameter affecting the output response is found to be first as the injection pressure, followed by engine load and WPO + diesel fuel blend.

  4. It is found from sensitivity analysis that the sensitivity of BTE to the injection pressure increases slightly with an increase in fuel blend percentage and sensitivity of NOx emission to the load decreases with increases in the fuel blend percentage.

  5. The highest value of BTE and the lowest value of NOx emission after the optimisation are found to be BTE at 32.5605 and NOx emission at 14.8757, respectively.

  6. The developed regression model from the RSM approach predicted accurately with average percentage errors of 1.3% and 8.2% when compared with the experimental value of BTE and NOx emission, respectively.

  7. The confirmatory tests are carried out to validate the optimised input operational parameters developed by using the desirability function approach. The findings are within the 95% permissible limits.

    In terms of primarily scientific discoveries,

    1. The reliability of the regression model in predicting the engine behaviour is substantiated by diagnostic diagrams and statistical analyses.

    2. The fuel blend, injection pressure, and engine load have a substantial impact on BTE and NOx emissions as exhibited by contour and three-dimensional surface plots.

    3. By incorporating multiple responses via desirability functions, the optimisation procedure generates optimal parameter values which culminate to enhanced BTE and reduced NOx emissions.

    4. By demonstrating how variations in the fuel blend, injection pressure, and load impact BTE and NOx emissions, sensitivity analyses offer valuable insightful evidence regarding the optimisation model’s reliability.

In accordance with the implications concerning the discipline:

  1. The investigation enhances the area by presenting an exhaustive comprehensive methodology for optimising CRDi diesel engines, taking into account both environment and performance considerations.

  2. By repurposing plastic waste, the use of WPO as a fuel source illustrates the sustainability of the environment.

  3. Future engine optimisation studies may be influenced by the regression model as well as optimisation strategies which have been developed, with a particular emphasis on reducing emissions and enhancing the efficiency.

11 Future outlook

  1. In future, other optimisation methods like WASPASS can be used, and data can be analysed using a meta-heuristic approach. The optimisation studies using the WPO derived from other plastic designs (mixture and individual) can be performed and compared with the work presented in this study.

  2. Examine the long-lasting implications of WPO–diesel fuel blends in the reliability as well as the durability of engines.

  3. Determine whether the developed optimisation model is applicable to different engine configurations and size capabilities.

  4. Evaluate the scalability, financial sustainability, along with economic viability of incorporating WPO into diesel engine applications on a broader scale.

  5. Further expand the scope of the investigation to include operational parameters that have the potential to impact engine performance and emissions.

  6. Investigate the possibility of incorporating advanced sophisticated control strategies in conjunction with optimised operational parameters to enable real-time instantaneous modifications to the engine performance.



Acknowledgment

Researchers Supporting Project number (RSPD2024R576), King Saud University, Riyadh, Saudi Arabia.

  1. Funding information: Researchers Supporting Project number (RSPD2024R576), King Saud University, Riyadh, Saudi Arabia.

  2. Author contributions: Conceptualisation: SK, MP, PK, RC, SP, RK, and SS; formal analysis: SK, MP, PK, RC, SP, RK, SS, FAA, and MIK; investigation: SK, MP, PK, RC, SP, RK, and SS; writing – original draft preparation: SK, MP, PK, RC, SP, RK, and SS; writing – review and editing: SS, FAA, MIK, and EAAI; supervision: SS, FAA, MIK, and EAAI; work administration: SS, FAA, MIK, and EAAI; funding acquisition: SS, FAA, MIK, and EAAI. All authors have read and agreed to the published version of the manuscript.

  3. Conflict of interest: The authors state no conflict of interest.

  4. Data availability statement: The datasets generated during and/or analysed during the current study are available from the corresponding author on reasonable request.

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Received: 2023-08-24
Accepted: 2023-12-04
Published Online: 2024-07-26

© 2024 the author(s), published by De Gruyter

This work is licensed under the Creative Commons Attribution 4.0 International License.

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