Environmental Risk Mitigation by Biodiesel Blending from Eichhornia crassipes : Performance and Emission Assessment

: The aggressive growth of Eichhornia crassipes (Water Hyacinth) plants causes severe damage to the irrigation, environment, and waterway systems in Iraq. This study aims to produce, characterize, and test biofuel extracted from the Eichhornia crassipes plant in Iraq. The extracted biodiesel was mixed at 10%, 20%, and 40% with neat diesel to produce three biodiesel samples. The methodology consists of the physiochemical properties of the samples that were characterized. The performance of the IC engine fueled by neat and biodiesel samples was measured under various operational conditions. The exhaust gases were analyzed to estimate the compounds to assess the environmental impact. The results showed that the density and viscosity of mixtures increase and the caloriﬁc value decrease with biodiesel. The engine test showed that the diesel + 10BE, diesel + 20BE, and diesel + 40BE enhanced brake thermal efﬁciency using 2.6%, 4.2%, and 6.3%, respectively, compared to neat diesel. Exhaust tests show a slight reduction, of 0.85–3.69% and 2.48–6.93%, in CO and HC emission, respectively. NOx is higher by 1.87–7.83% compared with neat diesel. The results revealed that biodiesel blended from Eichhornia crassipes is a viable solution to mitigate the drastic impact on the environment and economy in Iraq. The blended biodiesel has good potential to be mixed with the locally produced diesel from oil reﬁneries.


Background and Research Literature
Oil and natural gases, which are depleting resources, represent the main economic pillar of Iraq and the main source of energy for power production and transportation. Meanwhile, emissions caused by combustion have considerably increased environmental pollution in the country [1]. In the last few years, scientists in Iraq have directed their interests in discovering alternatives to fossil fuels. One of these alternatives is vegetable oils to produce biofuels as renewable energy, which is environmentally friendly, renewable, and biodegradable [2,3]. Biodiesel is a better lubricant than diesel oil that lengthens engine life. Several vegetable oils, such as castor, sunflower, and palm trees, are available in Iraq. However, all these vegetable oils have high values and important uses other than biodiesel production. A certain raw material must be readily available during selection. Also, it must not be useful for another purpose rather than being used for biodiesel production. Hirkude and Padalkar [4] have reported waste-fried oil methyl ester blend and [5] reported biodiesel production from used cooking oil. Benjumea et al. [6,7] characterized and reported biodiesel blended from palm oil. In contrast, the authors of [8] have reported their experimental result about a diesel engine's performance and emission assessment fueled with methyl chloroformates of a rubber seed oil.
Eichhornia crassipes (E. crassipes), also named Water Hyacinth, has been a source of interest in recent studies to blend and characterize biodiesel. In their review article, the

Eichhornia Crassipes (Water Hyacinth) in Iraq
The presence of E. Crassipes in water bathmats slows down water flow and leads to sludging. Reduced water flow adversely affects irrigation systems. Investigations demonstrated that this water plant causes considerable loss of water resources through evapotranspiration.
The E. crassipes is an aquatic plant that can tolerate a wide range of habitat conditions (e.g., winds, temperature, pH, salinity, current, and drought), as shown by [16,17]. It grows in fresh water at an optimal pH 7.0, a phosphorus concentration of 20 ppm, and adequate nitrogen. It can also survive up to 13 days in seawater and has features that make it well adapted for long-distance dispersal and the successful colonization of diverse habitats. The E. crassipes reduce the effective capacity of water reservoirs by up to 400 m 3 of water per hectare. A dry climate, such as that in Iraq, causes water levels in reservoirs to fall quickly, thereby causing a major impact on the hydroelectric structures of water reservoirs and streams. Traveling using boats becomes difficult or impossible because of E. crassipes, thereby resulting in water transport problems.
In recent years, rivers and irrigation water streams in Iraq have been suffering from the rapid and wide growth of E. crassipes plants because it inhibits water flow in the Tigris and Euphrates rivers and their tributaries in the provinces of Wasit and Dhi-Qar. Figure 1 shows the distribution of the E. crassipes plant in the rivers of Iraq. The quantitative statistics of the water hyacinth plant extracted by the Directorate of Aquatic Treatment indicate that the quantities increased from 350 sq. km in 2006 to 860 sq. km in 2016 in the southern part of Iraq. This condition led the authorities in charge of water resources to pay high costs to remove these plants from the rivers without benefiting them.  As for the sustainability and supply chain, the areas rich with E. crassipes with massive scale availability are shown as green dots in Figure 1. These are concentrated in the southern and eastern parts of Iraq. The process and optimization of the exhaustive supply chain could be assimilated utilizing the model proposed by [18].

Motivation and Research Objective
The aggressive growth of the E. crassipes plant causes severe environmental and socioeconomic problems in Iraq. This plant represents a strong promise in the biofuel industry due to its fast growth with no human nursing or attention. Hence, the motivation of the current research is to assess the validity of the potential use of extracted biodiesel from E. crassipes as added biofuel to the neat diesel produced in Iraqi refineries. This research is the first attempt to produce biodiesel from the E. crassipes plant in Iraq and assess its technical and environmental characteristics. In addition to pure diesel, three mixed blends were prepared and subjected to characterization and evaluation as fuel for internal combustion (IC) engines. Each mixture consisted of neat diesel (D) and 10%, 20%, and 40% by volume of biofuel blended with E. crassipes. Investigation results are presented as fuel blend characteristics, engine performance at various operational conditions, and exhaust gas analysis to assess the environmental impact. The growth of E. crassipes plants in Iraqi water streams and rivers represents a severe problem to the health, fishery, and agriculture industries in Iraq. The massive growth of E. crassipes plants affects the environment and various socioeconomic factors in Iraq. Unfortunately, this harsh plant is not utilized by any means in Iraq and the Middle Eastern region.
As for the sustainability and supply chain, the areas rich with E. crassipes with massive scale availability are shown as green dots in Figure 1. These are concentrated in the southern and eastern parts of Iraq. The process and optimization of the exhaustive supply chain could be assimilated utilizing the model proposed by [18].

Motivation and Research Objective
The aggressive growth of the E. crassipes plant causes severe environmental and socioeconomic problems in Iraq. This plant represents a strong promise in the biofuel industry due to its fast growth with no human nursing or attention. Hence, the motivation of the current research is to assess the validity of the potential use of extracted biodiesel from E. crassipes as added biofuel to the neat diesel produced in Iraqi refineries. This research is the first attempt to produce biodiesel from the E. crassipes plant in Iraq and assess its technical and environmental characteristics. In addition to pure diesel, three mixed blends were prepared and subjected to characterization and evaluation as fuel for internal combustion (IC) engines. Each mixture consisted of neat diesel (D) and 10%, 20%, and 40% by volume of biofuel blended with E. crassipes. Investigation results are presented as fuel blend characteristics, engine performance at various operational conditions, and exhaust gas analysis to assess the environmental impact.

Biodiesel Production Procedure
In the current investigations, biofuel ethanol was produced in two steps: saccharification and fermentation. The stationary fermentation method was adopted. For saccharification, intact fungal organism Aspergillums Niger was used as a source of cellulose enzyme. The plant is shown in Figure 2.

Biodiesel Production Procedure
In the current investigations, biofuel ethanol was produced in two steps: saccharification and fermentation. The stationary fermentation method was adopted. For saccharification, intact fungal organism Aspergillums Niger was used as a source of cellulose enzyme. The plant is shown in Figure 2. Leaves, petioles, and roots were separated from the E. crassipes plant. The roots were discarded because they absorb heavy metal pollutants from water. The leaves and petioles were washed manually with tap water and distilled water to remove any solid particles. Subsequently, they were sundried and pre-treated with 1.0% NaOH for two hours. About 30 kg was brought from the site to the University of Technology for characterizations and testing.
To characterize the bio composition of the plant, the following procedure has been followed [19]:  A small amount of the stems and leaves were taken to the chemical department laboratory for bio composition characterization. The small amount was rinsed with distilled water and left to dry at room temperature. The sample was further dried in an electric oven at 110 °C for a day to remove the moisture.  The dry sample was ground into powder using a grinding mill, and the particles were sieved using a 300 μm standard sieve.  A sample of 100 g of the powder was tested by Fourier transform infrared spectroscopy (FTIR) machine. The wavelength resultant was compared to a standard chart to identify the percentage of cellulose, hemicellulose, and lignin.
The test results are shown in Table 1.  Leaves, petioles, and roots were separated from the E. crassipes plant. The roots were discarded because they absorb heavy metal pollutants from water. The leaves and petioles were washed manually with tap water and distilled water to remove any solid particles. Subsequently, they were sundried and pre-treated with 1.0% NaOH for two hours. About 30 kg was brought from the site to the University of Technology for characterizations and testing.
To characterize the bio composition of the plant, the following procedure has been followed [19]: • A small amount of the stems and leaves were taken to the chemical department laboratory for bio composition characterization. The small amount was rinsed with distilled water and left to dry at room temperature. The sample was further dried in an electric oven at 110 • C for a day to remove the moisture.

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The dry sample was ground into powder using a grinding mill, and the particles were sieved using a 300 µm standard sieve. • A sample of 100 g of the powder was tested by Fourier transform infrared spectroscopy (FTIR) machine. The wavelength resultant was compared to a standard chart to identify the percentage of cellulose, hemicellulose, and lignin.
The test results are shown in Table 1. To blend the diesel from the 30 kg of E. crassipes, 6.0 wt.% sulfuric acid catalyst and a methanol-to-oil ratio of 5:1 was processed in a hydrodynamic cavitation reactor at 60 • C using circulating liquid glycerin for 45 min, as recommended by [17]. A hydrodynamic Sustainability 2021, 13, 8274 5 of 16 cavitation reactor with 50 L capacity was used to produce E. crassipes oil biodiesel. The reactor consisted of a diaphragm pump, double-jacked glass, and air compressor to operate the double diaphragm pump, which acted as a device to dissipate the energy in the hydrodynamic cavitation reactor [20][21][22]. Outlines of the laboratory production of biodiesel from E. crassipes plant are presented in Figure 3. methanol-to-oil ratio of 5:1 was processed in a hydrodynamic cavitation reactor at 60 °C using circulating liquid glycerin for 45 min, as recommended by [17]. A hydrodynamic cavitation reactor with 50 L capacity was used to produce E. crassipes oil biodiesel. The reactor consisted of a diaphragm pump, double-jacked glass, and air compressor to operate the double diaphragm pump, which acted as a device to dissipate the energy in the hydrodynamic cavitation reactor [20][21][22]. Outlines of the laboratory production of biodiesel from E. crassipes plant are presented in Figure 3.
Mixtures of fuel blends were prepared from diesel and blended biodiesel from E. crassipes (BE). The mixture consisted of 90% D and 10% BE by vol. (D + 10BE). The second fuel blend contained 80% D and 20% BE by vol. (D + 20BE), and the third fuel blend contained 60% D and 40% BE by vol. (D + 40 BE). These samples were subsequently used to fuel the experimental diesel engine setup to measure their performance and emission characteristics.

Diesel and Biodiesel Characterization
The physiochemical properties of the four fuel samples, D, D + 10BE, D + 20BE, and D + 40BE, were measured following the ASTM and EN standards fuel characterization procedure. The standard procedures followed for the characterization and the equipment, with their accuracies, are as below: Mixtures of fuel blends were prepared from diesel and blended biodiesel from E. crassipes (BE). The mixture consisted of 90% D and 10% BE by vol. (D + 10BE). The second fuel blend contained 80% D and 20% BE by vol. (D + 20BE), and the third fuel blend contained 60% D and 40% BE by vol. (D + 40 BE). These samples were subsequently used to fuel the experimental diesel engine setup to measure their performance and emission characteristics.

Diesel and Biodiesel Characterization
The physiochemical properties of the four fuel samples, D, D + 10BE, D + 20BE, and D + 40BE, were measured following the ASTM and EN standards fuel characterization procedure. The standard procedures followed for the characterization and the equipment, with their accuracies, are as below: Density: Anton Paar Densometer (model DMA 4500M with a resolution of 0.00001 g/cm 3 and accuracy of 0.000005 g/cm 3 ) was used to measure density following the ASTM D-5002 standard method. Viscosity: Anton Paar Lovis rolling ball viscometer (model 2000 M/ME with viscosity measuring range of 0.3 mPa.s to 10,000 mPa.s and accuracy of up to 0.5% of the reading) was used to measure viscosity according to the 2000M/ME method. Flashpoint was obtained using a CPP 5Gs analyzer, with an accuracy of 0.1 • C, following the ASTM D-2500 procedure. Pour point temperatures were found using a CPP 5G analyzer, with an accuracy of 0.1 • C following the ASTM D-97 testing procedure. Cold filter plugging point was obtained using an FPP 5Gs analyzer, with two infrared detection barriers, following the ASTM D-6371 standard test procedure. The Oxidation stability was obtained using an 873-CH-9101 Metrohm analyzer, with an accuracy of 0.3 • C, following EN-14112 standard testing procedure. The Cetane number was analyzed using SHATOX SX-100K equipment, with 1.0 Cetane level measurement error, following the ASTM D-613 standard method. Ramé-hart, Model 260, with an accuracy of ±0.10 • , was used to measure the surface tension according to the pendant drop method. Pregl-Dumas method was adopted to determine the diesel contents of Carbon, Nitrogen, Hydrogen, and Oxygen by CHNS analyzer. Gas chromatography with the flame ionization detector has been used to determine the fatty acid components.

Experimental Setup
The experimental setup utilized in the current investigations consisted of a diesel engine type TWD290F with a BEA 460 Bosch gas analyzer supplied with specialized software for data acquisition attached to the engine exhaust. The experimental setup is shown schematically in Figure 4. The combustion performance was achieved using a direct injection single-cylinder diesel engine with specifications provided in Table 2.

Uncertainty Analysis
Error analysis in the experiments is essential to provide a level of confidence in the results. It could be achieved by determining the repeatability and reproductivity of the results. All experiments were repeated thrice. The variants of the predicted values of performance factors and exhaust emissions were used to calculate the uncertainty using the percent relative standard error, ∅, as shown in Equation (1):  The experimental system enables measurement of engine speed, engine torque, fuel flow rate, airflow rate, and all relevant temperatures and pressures. The software automatically optimizes the gas analysis. The experiments were performed at an engine speed of 2000 RPM at different throttling positions (20-100%). The engine's maximum power is 6.6 kW at 3200 RPM.
Experiment data were recorded after around 4 min of the starting or changing operation status, where the engine reached a stabilized operation status. The measurements were performed at steady-state operational conditions.

Uncertainty Analysis
Error analysis in the experiments is essential to provide a level of confidence in the results. It could be achieved by determining the repeatability and reproductivity of the results. All experiments were repeated thrice. The variants of the predicted values of performance factors and exhaust emissions were used to calculate the uncertainty using the percent relative standard error, ∅, as shown in Equation (1): where SE is the standard error, and Y is the mean of the collected data. The standard error is calculated using Equation (2): where σ is the standard deviation, and k is the repeatable readings of performance, combustion characteristics, and emission parameters.
Overall experimental uncertainty, σ n , was calculated using Equation (3): where σ n is the total uncertainty, and σ 1 , σ 2 , and σ i are the uncertainties of the individual parameters.
The accuracies and uncertainties of the measured parameters are given in Table 3.

Thermodynamic Analysis
Thermodynamic analyses were carried out for a full load (engine throttle positioned at 100%) at maximum power, which the engine presents at 2000 RPM. Energy and exergy analyses were used, and the first and second law efficiencies were obtained. The overall engine was assumed to be a control volume with a steady-state open system, as shown in Figure 5. In this analysis, air and fuel charges were entered into the engine, and exhaust gas charges exited from the system boundary after losing heat and work. The inlet air and exhaust gases were acceptably presumed as ideal gases. The environmental conditions were considered as 1 atm and 25 • C. The kinetic and potential energy were neglected for fuel, air, and exhaust.

Thermodynamic Analysis
Thermodynamic analyses were carried out for a full load (engine throttle positioned at 100%) at maximum power, which the engine presents at 2000 RPM. Energy and exergy analyses were used, and the first and second law efficiencies were obtained. The overall engine was assumed to be a control volume with a steady-state open system, as shown in Figure 5. In this analysis, air and fuel charges were entered into the engine, and exhaust gas charges exited from the system boundary after losing heat and work. The inlet air and exhaust gases were acceptably presumed as ideal gases. The environmental conditions were considered as 1 atm and 25 °C. The kinetic and potential energy were neglected for fuel, air, and exhaust. The molar rate and fractions were estimated from the combustion equation. Fuel and airflow rates were measured experimentally, and the emissions, including CO2, CO, NO, and HC, were known. Hence, the residual species' molar rates could be determined. Consequently, all molar rates could be placed in the combustion equation. NO2 was not observed in the emissions, and PM has been neglected since they were sufficiently low [23].

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The thermomechanical and chemical exergy of the air and fuel were ignored at the inlet because fuel and air enter the control volume as reference state conditions. Therefore, only the chemical exergy factor ∅ of fuel was evaluated as follows: Herein, x1, x2, x3, x4 are the mass fractions of hydrogen, oxygen, carbon, and sulfur of liquid fuel, respectively. The overall chemical exergy of fuel is: The power output was taken from experimental results. The power was predicted from the measured torque and speed, using Equation (7): 2 60 (7) The molar rate and fractions were estimated from the combustion equation. Fuel and airflow rates were measured experimentally, and the emissions, including CO 2 , CO, NO, and HC, were known. Hence, the residual species' molar rates could be determined. Consequently, all molar rates could be placed in the combustion equation. NO 2 was not observed in the emissions, and PM has been neglected since they were sufficiently low [23].
The thermomechanical and chemical exergy of the air and fuel were ignored at the inlet because fuel and air enter the control volume as reference state conditions. Therefore, only the chemical exergy factor ∅ of fuel was evaluated as follows: Herein, x 1 , x 2 , x 3 , x 4 are the mass fractions of hydrogen, oxygen, carbon, and sulfur of liquid fuel, respectively. The overall chemical exergy of fuel is: .
The power output was taken from experimental results. The power was predicted from the measured torque and speed, using Equation (7): Q exh , was evaluated from the thermodynamic tables, as per [23], considering each emission gas species' enthalpy values and molar flow rate, as in Equation (8): Heat losses exit from control volume is calculated from the difference between the inlet and exit energy. Herein, the air energy was ignored since it enters as reference state temperature: The exergy of the exhaust gases, exh , is the sum of thermomechanical and chemical exergies species. The thermomechanical exergy, exh , was evaluated from thermodynamic tables for each species as follows: The chemical exergy in the exhaust gases, chem , was evaluated using standard molar chemical exergy, η ch table, Model II by [24] and using molar fractions, ψ, as follows: The exhaust exergy rate can be defined as the sum of the chemical and the thermomechanical exergy multiplying molar rates: The work exergy rate is equal to the power output: .
The heat loss exergy, which consists of friction, radiation, and cooling water losses, etc., was assumed, in actuality, to occur from the 363 K engine cylinder block to the 298 K reference environment [25]. The heat loss exergy rate can be defined as: The exergy destruction rate is obtained from the exergy balance and the difference between the inlet and outlet exergies as follows: Therefore, the first law efficiency is obtained as the ratio of the power output, W, to the fuel energy rate, Q in , in Equation (16): The second law efficiency, which is referred to as exergetic efficiency, could be estimated using Equation (17):

Results and Discussion
The acquired data from the experimental measurements were clustered to highlight the effect of the added biodiesel on the pure diesel. One batch of results presents the influence of the added biodiesel on the performance of the IC engine. The second batch of results presents the exhaust gas analysis and the emissions, which are important for the environmental consequences.

Characterization Results
The mixtures of neat diesel and biodiesel have been characterized as described in Section 2.2. The properties of diesel and the blends are presented in Table 4. The trend of the characteristic changes with the addition of biodiesel to the neat diesel is similar to the data of [13]

Heat Release Rate
The gross amount of heat release rate (HRR) is the sum of the heat transfer to the chamber of the cylinder and the net heat transfer. The estimation accuracy of the HRR depends on many factors such as the accurate measurement of the in-cylinder pressure, the accurate determination of the TDC location, and the assumptions adopted in the HRR prediction model. The heat release model proposed by Krieger and Borman [26] is adopted in the current investigation. Specific heat ratios are considered as constant at 1.35. Figure 6 presents the measured heat release rates under different fuel mixtures at various crank angles at maximum power. The combustion start timing could not be determined precisely as all results are taken in 720 • CA. However, it can be said that more fuel ignited at the beginning of the combustion for D + 40BE, and the ignition delay is longer for D + 10BE compared to neat diesel fuel. A higher Cetane number is found in D + 40BE, and a high viscosity and density are dominant for D + 10BE, corresponding with engine geometry.  Figure 7 shows the in-cylinder maximum pressure results. Later ignition causes lower pressure due to expansion and cooling for D + 10BE. The D + 40BE fuel blend has Moreover, the results presented in Figure 4 display the peak heat release rates. The maximum heat release rate is reached by suddenly burning D + 10BE, which is waiting before ignition. The test engine produces its maximum torque at 2000 rpm. The cases of diesel-biodiesel experimented by [13] have shown lower HRR than pure diesel. Figure 7 shows the in-cylinder maximum pressure results. Later ignition causes lower pressure due to expansion and cooling for D + 10BE. The D + 40BE fuel blend has nearly higher peak pressures than pure diesel fuel except at high engine rotational speeds, 2700 and 3000 rpm, as the reason mentioned above. The cetane number dominates, and early ignition increases the pressure with a higher Cetane number. D + 20BE generally has similar results with pure diesel fuel.  Figure 7 shows the in-cylinder maximum pressure results. Later ignition causes lower pressure due to expansion and cooling for D + 10BE. The D + 40BE fuel blend has nearly higher peak pressures than pure diesel fuel except at high engine rotational speeds, 2700 and 3000 rpm, as the reason mentioned above. The cetane number dominates, and early ignition increases the pressure with a higher Cetane number. D + 20BE generally has similar results with pure diesel fuel.

Brake Thermal Efficiency
The brake thermal efficiency (BTE) has been adopted as a performance indicator. The variation of BTE, for the four fuel samples with their blends, D, D + 10BE, D + 20BE, and D + 40BE, at varying loading conditions is presented in Figure 8. The break efficiency of D, D + 10BE, D + 20BE, and D + 40BE fuels increases with the load by up to approximately 90% loading condition, and then begins to decrease.

Brake Thermal Efficiency
The brake thermal efficiency (BTE) has been adopted as a performance indicator. The variation of BTE, for the four fuel samples with their blends, D, D + 10BE, D + 20BE, and D + 40BE, at varying loading conditions is presented in Figure 8. The break efficiency of D, D + 10BE, D + 20BE, and D + 40BE fuels increases with the load by up to approximately 90% loading condition, and then begins to decrease. At high loading conditions, the D + 40BE blend shows the highest BTE among all other samples since the increase in the biodiesel ratio reduces the volumetric heating value of the blend, thereby causing a decrease in brake power. In addition, the high density and viscosity have resulted in uneven combustion, reducing the brake power [25]. At high loading conditions, the D + 40BE blend shows the highest BTE among all other samples since the increase in the biodiesel ratio reduces the volumetric heating value of the blend, thereby causing a decrease in brake power. In addition, the high density and viscosity have resulted in uneven combustion, reducing the brake power [25]. Figure 9 shows the BSFC changing trend at various engine loads. The BSFC decreased with the increase in engine load for all of the tested fuel samples, thereby demonstrating good combustion. The D + 10BE, D + 20BE, and D + 40BE fuel blends exhibited higher fuel consumption than diesel at all loading conditions. The increase in the BSFC resulted from the low heating value and the high viscosity and density, thereby causing a greater amount of fuel to be injected into the combustion chamber than the D fuel [25]. These results are consistent with the findings of [26][27][28]. At high loading conditions, the D + 40BE blend shows the highest BTE among all other samples since the increase in the biodiesel ratio reduces the volumetric heating value of the blend, thereby causing a decrease in brake power. In addition, the high density and viscosity have resulted in uneven combustion, reducing the brake power [25]. Figure 9 shows the BSFC changing trend at various engine loads. The BSFC decreased with the increase in engine load for all of the tested fuel samples, thereby demonstrating good combustion. The D + 10BE, D + 20BE, and D + 40BE fuel blends exhibited higher fuel consumption than diesel at all loading conditions. The increase in the BSFC resulted from the low heating value and the high viscosity and density, thereby causing a greater amount of fuel to be injected into the combustion chamber than the D fuel [25]. These results are consistent with the findings of [26][27][28].

Environmental Assessment Results
The consequences of adding biodiesel to the neat diesel changes the chemical composition of the mixture. Hence, the exhaust gases are changing in terms of emission. The resulting HC, CO, and NOx have been measured to evaluate the emission characteristics. All of the characterization parameters have been evaluated at different loading conditions of the test engine, varying from a 20% load to a 100% full load.

Environmental Assessment Results
The consequences of adding biodiesel to the neat diesel changes the chemical composition of the mixture. Hence, the exhaust gases are changing in terms of emission. The resulting HC, CO, and NOx have been measured to evaluate the emission characteristics. All of the characterization parameters have been evaluated at different loading conditions of the test engine, varying from a 20% load to a 100% full load. Figure 10 displays the CO emission of neat diesel and a mixture of diesel and bio blends at various engine loads. Results show that the CO emissions increase with the engine load because CO emissions are extremely dependent on the air-fuel ratio [13,17]. In addition, the results revealed that CO emission is the highest in neat diesel, followed by D + 10BE, D + 20BE, and D + 40BE fuel blends in all cases of the loading conditions. This effect is evident during full loading conditions but is not so vital at low loads because of their low values. The decrease in CO emissions for the D + 10BE, D + 20BE, and D + 40BE fuel blends may be attributed to the added oxygen percentage in the fuel blend, thereby confirming the remarkable combustion of the fuel. Refs. [12][13][14] also claimed similar results of slight reductions of CO percentages in the exhaust gasses of their testing engines using the various percentages of diesel with E. crassipes blends. As experienced by [13], the current investigation demonstrates that the CO of diesel fuel is higher than the mixtures of diesel with biodiesel at all engine loadings. This is due to oxygen deficiency in diesel fuel overriding the mixtures which have intrinsic fuel oxygen content. The presence of O 2 in the fuel enhances the combustion rate and encourages the faster switch of CO to CO 2 .
sults of slight reductions of CO percentages in the exhaust gasses of their testing engines using the various percentages of diesel with E. crassipes blends. As experienced by [13], the current investigation demonstrates that the CO of diesel fuel is higher than the mixtures of diesel with biodiesel at all engine loadings. This is due to oxygen deficiency in diesel fuel overriding the mixtures which have intrinsic fuel oxygen content. The presence of O2 in the fuel enhances the combustion rate and encourages the faster switch of CO to CO2. The variation of NOx emission at various engine loads of the considered fuel blends is shown in Figure 11. The engine load increased with the increase in NOx emission. However, the values of the NOx emissions for D + 10BE, D + 20BE, and D + 40BE are above that of pure diesel. Khan et al. [12] also observed slightly higher NOx. The variation of NOx emission at various engine loads of the considered fuel blends is shown in Figure 11. The engine load increased with the increase in NOx emission. However, the values of the NOx emissions for D + 10BE, D + 20BE, and D + 40BE are above that of pure diesel. Khan et al. [12] also observed slightly higher NOx. HC emission at various engine loads for the studied fuel blends is presented in Figure 12. The HC emission changes are similar to the CO emission. Thus, HC emission is the highest for diesel and lessens for the fuels D + 10BE, D + 20BE, and D + 40BE fuel blends. The reasons for such comportment of HC emission are described in CO emission. The low carbon-to-hydrogen ratio and oxygen component in biodiesel fuels have caused improved combustion, reducing HC emissions [29,30]. HC emission at various engine loads for the studied fuel blends is presented in Figure 12. The HC emission changes are similar to the CO emission. Thus, HC emission is the highest for diesel and lessens for the fuels D + 10BE, D + 20BE, and D + 40BE fuel blends. The reasons for such comportment of HC emission are described in CO emission. The low carbon-to-hydrogen ratio and oxygen component in biodiesel fuels have caused improved combustion, reducing HC emissions [29,30].
HC emission at various engine loads for the studied fuel blends is presented in Figure 12. The HC emission changes are similar to the CO emission. Thus, HC emission is the highest for diesel and lessens for the fuels D + 10BE, D + 20BE, and D + 40BE fuel blends. The reasons for such comportment of HC emission are described in CO emission. The low carbon-to-hydrogen ratio and oxygen component in biodiesel fuels have caused improved combustion, reducing HC emissions [29,30].

Conclusions
The current research aims to assess the suitability of blended biofuel from E. crassipes plant as an additive to neat diesel in Iraq. The combustion performance and emissions characteristics of biofuel produced from the E. Crassipes plant, and their biodiesel blends have been investigated and compared with neat diesel as baseline fuels. The physicochemical properties of all the considered fuel samples (e.g., D, D + 10BE, D + 20BE, and D +

Conclusions
The current research aims to assess the suitability of blended biofuel from E. crassipes plant as an additive to neat diesel in Iraq. The combustion performance and emissions characteristics of biofuel produced from the E. Crassipes plant, and their biodiesel blends have been investigated and compared with neat diesel as baseline fuels. The physicochemical properties of all the considered fuel samples (e.g., D, D + 10BE, D + 20BE, and D + 40BE) are measured according to the ASTM standards. The following conclusions are drawn based on the obtained results: • Fuel properties: The density and viscosity of the fuel blend increase, and the calorific value decreases with the addition of biofuel.

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The engine performance of IC has been enhanced with the addition of E. crassipes biofuel. Compared with the neat diesel, the biodiesel blend of D + 10BE, D + 20BE, and D + 40BE enhanced brake thermal efficiency by 2.6%, 4.2%, and 6.3%, respectively.

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The reduction percentage of CO is 0.85-3.69% and 2.48-6.93% of HC compared with the neat diesel. The increasing percentage of NOx compared with pure diesel is 1.87 to 7.83%.

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The assessment results of 40% biofuel extracted from the E. crassipes and mixed with neat diesel demonstrate a remarkable effect on the engine performance with reduced emission.
The results encourage using the E. crassipes biodiesel blend as an additive to the commercial diesel in Iraq as a potential application. In addition, it resolves the problem of dealing with these plants, as the current practice is to dry the harvested plants under open solar drying. This practice would never eliminate the problem as the seeds survive and grow on a larger scale. Further investigations using different types and amounts of surfactant added to the diesel fuel and blends are recommended.