# Fast Rate Production of Biodiesel from Neem Seed Oil Using a Catalyst Made from Banana Peel Ash Loaded with Metal Oxide (Li-CaO/Fe2 (SO4)3)

Authors: Ismail J. Madai; Yusufu Abeid Chande Jande; Thomas Kivevele
Journal: Advances in Materials Science and Engineering
 (2020)

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## Abstract

Biodiesel is a possible remedy to the present toxic, finite sources and ever-diminishing crude fuels. Nonedible and locally available (Azadirachta indica) neem seed oil (NSO) as a second-generation feedstock was transformed into biodiesel using calcined banana ash (CBA) derived from banana peels blended with lithium calcium oxide iron (III) sulphate Li-CaO/Fe2 (SO4)3 catalyzed transesterification. Transesterification process was employed to minimize the free fatty acid (FFA) content of NSO to afford 99.8% yield under the condition of the reaction oil/methanol ratio 8 : 1, followed by addition of 1.7%wt calcined banana peels ash and 1.3%wt Li-CaO/Fe2(SO4)3 catalysts in 53 min, a notable time. It is important to note that the physicochemical properties of biodiesel in this study such as initial boiling points, flash point, pour point, cloud point, density, kinematic viscosity, final boiling points, and cetane index met ASTM D-6751 and EN 14214 standards. Decomposition profile of CBA was displayed by thermal gravimetric analysis (TGA), whereas in-depth analysis by scanning electron microscope (SEM), X-ray diffraction (XRD), X-ray fluorescence (X-RF), and Fourier-transform infrared spectroscopy (FT-IR) revealed that the high efficiency displayed by a catalyst from banana ash calcined at 650°C was due to the presence of potassium carbonate (K2CO3), a calcium magnesium silicate (CaMgSiO4), and potassium sodium sulphate (KNaSO4) contents that accounted for the high basicity of up to 11.09. Additionally, the nitrogen adsorption/desorption studies revealed that CBA interestingly exhibits a high BET surface area of 411.2 m2/g and promising mesopores (3.014 nm). The catalyst also displayed better recyclability evidenced by the fact that it was able to be reused after five successive runs with better recyclability of 75%. Based on the aforementioned properties, this work, therefore, opens an avenue for developing a supreme heterogeneous catalyst from available banana peels ash.


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## Body

## 1. Introduction

The current rate of depletion of fossil fuels accompanied by environmental pollution justifies the need for scientists to divert their attention to green and environmentally compatible energy sources. As one of the most targeted sources of energy, biodiesel has shown its supremacy by its ability to undergo degradation and it is also a renewable, affordable, and environmentally friendly source of energy [1]. Having been reported that direct use of plant oil can cause engine problems such as incomplete combustion, high carbon deposit on the combustion chamber, valve seat, and injector nozzle, therefore, biodiesel is a better option to curb these problems as shown by Ahmad et al. [2]. Transesterification is the main method that has been used in the production of biodiesel as shown by Meher et al. [3]. It is a reaction between oil and alcohol (methanol/ethanol) giving out compounds known as alkyl-esters (methyl/ethyl) accompanied by glycerol as a waste product as shown by Ghadge and Raheman [4]. The intact reaction minimizes parameters such as density, molecular weight, and viscosity and even draws its volatility close to that of diesel fuel by Coniglio et al. [5].For instance, oil from rapeseed (Ramos et al. [6]), soya beans (Gui et al. [7]), sunflower (Antolın [8]), and palm (Crabbe et al. [9]) has gained attention. Unfortunately, the use of edible oils poses a risk in food security and therefore, the current research trends are targeting nonedible oils as the second generation of biodiesel feedstock (Barnwal and Sharma [10]). Various nonedible seeds including neem seed, jatropha, croton, and castor beans have been studied and show good performance in biodiesel production (Atabani et al. [11]). Neem seeds are derived from unique neem trees that have a long lifespan estimated to lie between 150 and 200 years (Schmutterer [12]). It can bear fruits within 3 to 5 years and attains maximum productivity after 10 years and its oil content varies from 30 to 35% and from 35 to 40% for kernels and seeds, respectively (Kaura et al. [13]). These properties necessitate thinking of it as a suitable feedstock for biodiesel production. It is given that 7 to 8 kg of neem seed produces one litre of oil. It is also worth mentioning in this work that planting of neem trees will address not only energy challenges but also environmental challenges (Kumar and Navaratnam [14]).Various researches including but not limited to banana peels as biomass precursors for biodiesel production have been conducted. For instance, Betiku et al. [15] researched on Napoleon’s plumule oil using banana (species Musa gros michel) peels CBA calcined at 700°C for 4 hours with 58.812% potassium composition and Fe2(SO4)3 as a catalyst; the efficiency for biodiesel yield was 98.05% for 69-minute reaction time with 2 wt% catalyst dosage. Similarly, Gohain et al. [16] used CBA from banana (species Musa paradisiacal) plantain peel from West Africa calcined at 700°C for 4 hours with 51.02% potassium composition as a catalyst alongside waste cooking oil and produced 96.3% of biodiesel for 60-minute reaction time with 7.6 wt% catalyst dosage.The previous application of banana peels as a catalyst for biodiesel production tends to be a slow, time-consuming, large dosage of catalyst usage and large waste disposal. This is due to low potassium content as well as low basic strength which resulted from high calcined of CBA at 700°C which is close to the melting point (740°C) of potassium oxide [15, 16]. This calcination may lead to the reaction to take longer time and hence a large dosage of catalyst usage and large waste production. The efficiency of basic contents determines the time for the production of biodiesel.The common species of banana with high availability in Arusha Tanzania as well as East Africa isMusa acuminata Colla. These banana species are used as food but their peels are treated as wastes [17, 18]. These peels have high potassium contents which can be used as a biocatalyst for biofuel production [19]. However, using these peels will increase banana production as well as solving the energy problem.On top of that, this leads to come up with loading metal oxide Li-CaO/Fe2 (SO4)3 to CBA biocatalyst which forms a strong basic catalyst that increases the oxidation by converting free fatty acid to methyl esters and the performance of the catalyst as well as catalyst reusability. These make the catalyst to be more efficient and stand for an environmentally compatible catalyst for hastening biodiesel production as a possible substitute fuel raw material.


## 2. Materials and Methods

### 2.1. Materials

The ripe banana peels were sourced from the Tengeru market in Arusha, Tanzania. The reagents used were methanol (CH3OH) 99.8%, ethanol (C2H5OH) absolute, iron (III) sulphate (Fe2(SO4)3), lithium metal (Li), calcium oxide (CaO), phenolphthalein (POP) indicator, hydrochloric acid (HCl) 37%, and Wijis and iodine solution. All chemicals were supplied by Sigma-Aldrich and were used without further modification.


### 2.2. Preparation of CBA

Ripe banana peels were sliced into small pieces to accelerate the drying process. After washing with distilled water, banana peels were sundried for 7 days (turned from yellow to black colour; became light in weight, hard, and wrinkled) followed by oven-drying at 100°C for 6 h. Then, the dried banana peels were ashed in a box muffle furnace in the presence of air and finally milled and sieved to a fine powder. The resulting fine ash was annealed in varying temperatures at 100°C interval from 550 to 1050°C for 3 h to remove impurities [16]. Finally, the calcined ripe banana peel ash was ground and kept in a seal for further analysis.


### 2.3. Preparation of Heterogeneous Catalyst

Calcined banana ash was tested for basicity by dissolving 5 g of CBA/Li-CaO/Fe2(SO4)3 blends in 50 mL of distilled water using pH meter. The blended catalyst metal oxide Li-CaO/Fe2(SO4)3/CBA was prepared using 1.3 wt% of lithium calcium oxide (Li-CaO)/iron (III), sulphate (Fe2(SO4)3), and 1.7 wt% of CB [1]. Then, 80 mL of methanol was measured using a measuring cylinder and poured in a conical flask. The blended catalyst was dissolved in methanol with continuous stirring of 2700 rpm within 5 min. Then, the solution of the blended catalyst was ready and finally waited for further activity.


### 2.4. Characterization of the Heterogeneous Catalyst

Micrometrics instruments (ASP2020) were employed for nitrogen sorption studies. Functional groups in the sample such as calcined banana ash were analyzed by using Fourier-transform infrared (FT-IR) instrument. The model of FT-IR used in this study was Alpha Bruker ATR, the wavenumber ranging from 4000 to 1000 cm−1, and XRF for elemental analysis composition. Thermogravimetric analysis was used to show the decomposition profile of the sample. Approximately, 0.24 mg of the sample was subjected to a temperature range from 29°C to 800°C in a time interval of 5.38 to 78.48 min. TGA gives a clear indication that the calcined temperature should start at 650°C. Finally, the ground catalyst precursor was subjected to heat treatment in a box furnace for 3 h at 650°C.


### 2.5. Neem Seed Oil Preparation

Neem seeds were purchased from Bagamoyo, Iringa, and Singida regions in Tanzania. Initially, the seeds were washed with distilled water and then sundried for five days to remove moisture content, whereas other solid dirty impurities were removed by handpicking and winnowing processes [20]. Seeds were soaked in water for 24 h to remove husks and finally pressed using a hydraulic pressing machine to obtain the oil.


### 2.6. Biodiesel Production through Transesterification Process

Transesterification process of NSO to biodiesel (methyl esters) was carried out using 1.7 wt% of CBA loaded with Li-CaO/Fe2 (SO4)3, 100 mL methanol, and 800 mL of NSO. The blended catalyst (1.7 wt% CBA/Li-CaO/Fe2 (SO4)3) was mixed with 100 mL of methanol with continuous stirring at 2700 rpm for five minutes, which was finally followed by addition into 800 mL of NSO (warmed to 40°C) with continuous stirring until two immiscible layers of biodiesel (top layer) and glycerol (bottom layer) were formed. This reaction was performed in 2000 mL conical flask and took 53 min. The conical flask was covered with aluminium foil and temperature was monitored by a thermometer under a constant temperature of 60°C; above this temperature, methanol will be boiled which will reduce the production of biodiesel [21]. The experiment was carried in a water bath until two immiscible layers of biodiesel (top layer) and glycerol (bottom layer) were formed [22]. This transesterification reaction takes place in alcoholic condition (methanol) as the media for the reaction to take place in presence of catalyst which speeds up the reaction but remains unchanged at the end of the reaction [23]. Both separating funnel and filtration methods were employed to isolate the catalyst from the reaction mixture and finally, the filtrate was washed and dried with anhydrous sodium sulphate [24]. The process was repeated using the same filtrate catalyst up to the fifth run. The transesterification process was repeated by varying catalyst dosage from 1 to 1.7 wt% and methanol-to-oil molar ratio varies from 2 : 1 to 16. Finally, biodiesel produced was tested using phenolphthalein indicator where the colour changes from clear to pink at a pH of 8-9 and the universal indicator was also used where the colour changes from green to dark green at pH of 8-9. However, the percentage of biodiesel yield was calculated by weighing the mass of biodiesel produced over the mass of oil used times hundred [25]. This was calculated using(1)percentage biodiesel yield=weight of biodiesel obtainedweight of oil used×100.


### 2.7. Characterization of Biodiesel Properties

Fatty acid composition analysis for NSO was done using Gas Chromatography-Mass Spectrometry (GC-MS), Anton Paar Stabinger viscometer SVM 4001, and density meter DMI 5000. Anton Paar.com instruments were used to determine kinematic viscosity at 40°C and density of biodiesel at 15.5°C per ASTM D7042 standards. Pour point and cloud point were determined by test cabinet instruments, PSL Systemtechnik/product/pour point tester 45150 and ASTM D2500 cloud point testing. The flashpoint was determined with the aid of Pensky-Martens flash point tester, PMA 5, Anton-Paar.com instruments as per ASTM D93 standards. The approximation of various values of acid, iodine, and saponification was done through the titration method.


### 2.8. Recyclability of the Catalyst

Heterogeneous catalysts have gained fame as compared to homogeneous catalysts because of their reusability [26]. Therefore, the recyclability of the catalyst synthesized in this study was determined as follows. Methanol was used to wash the catalyst spent in the biodiesel production to remove the contents of glycerol and oil. Since water is a product of the transesterification process, the catalyst was later oven-dried for 2 h at a temperature of 110°C. After drying and cooling, the spent catalyst was successfully used to produce biodiesel for the next successive run. Biodiesel yield produced was calculated after every successful run till the fifth run.


## 2.1. Materials

The ripe banana peels were sourced from the Tengeru market in Arusha, Tanzania. The reagents used were methanol (CH3OH) 99.8%, ethanol (C2H5OH) absolute, iron (III) sulphate (Fe2(SO4)3), lithium metal (Li), calcium oxide (CaO), phenolphthalein (POP) indicator, hydrochloric acid (HCl) 37%, and Wijis and iodine solution. All chemicals were supplied by Sigma-Aldrich and were used without further modification.


## 2.2. Preparation of CBA

Ripe banana peels were sliced into small pieces to accelerate the drying process. After washing with distilled water, banana peels were sundried for 7 days (turned from yellow to black colour; became light in weight, hard, and wrinkled) followed by oven-drying at 100°C for 6 h. Then, the dried banana peels were ashed in a box muffle furnace in the presence of air and finally milled and sieved to a fine powder. The resulting fine ash was annealed in varying temperatures at 100°C interval from 550 to 1050°C for 3 h to remove impurities [16]. Finally, the calcined ripe banana peel ash was ground and kept in a seal for further analysis.


## 2.3. Preparation of Heterogeneous Catalyst

Calcined banana ash was tested for basicity by dissolving 5 g of CBA/Li-CaO/Fe2(SO4)3 blends in 50 mL of distilled water using pH meter. The blended catalyst metal oxide Li-CaO/Fe2(SO4)3/CBA was prepared using 1.3 wt% of lithium calcium oxide (Li-CaO)/iron (III), sulphate (Fe2(SO4)3), and 1.7 wt% of CB [1]. Then, 80 mL of methanol was measured using a measuring cylinder and poured in a conical flask. The blended catalyst was dissolved in methanol with continuous stirring of 2700 rpm within 5 min. Then, the solution of the blended catalyst was ready and finally waited for further activity.


## 2.4. Characterization of the Heterogeneous Catalyst

Micrometrics instruments (ASP2020) were employed for nitrogen sorption studies. Functional groups in the sample such as calcined banana ash were analyzed by using Fourier-transform infrared (FT-IR) instrument. The model of FT-IR used in this study was Alpha Bruker ATR, the wavenumber ranging from 4000 to 1000 cm−1, and XRF for elemental analysis composition. Thermogravimetric analysis was used to show the decomposition profile of the sample. Approximately, 0.24 mg of the sample was subjected to a temperature range from 29°C to 800°C in a time interval of 5.38 to 78.48 min. TGA gives a clear indication that the calcined temperature should start at 650°C. Finally, the ground catalyst precursor was subjected to heat treatment in a box furnace for 3 h at 650°C.


## 2.5. Neem Seed Oil Preparation

Neem seeds were purchased from Bagamoyo, Iringa, and Singida regions in Tanzania. Initially, the seeds were washed with distilled water and then sundried for five days to remove moisture content, whereas other solid dirty impurities were removed by handpicking and winnowing processes [20]. Seeds were soaked in water for 24 h to remove husks and finally pressed using a hydraulic pressing machine to obtain the oil.


## 2.6. Biodiesel Production through Transesterification Process

Transesterification process of NSO to biodiesel (methyl esters) was carried out using 1.7 wt% of CBA loaded with Li-CaO/Fe2 (SO4)3, 100 mL methanol, and 800 mL of NSO. The blended catalyst (1.7 wt% CBA/Li-CaO/Fe2 (SO4)3) was mixed with 100 mL of methanol with continuous stirring at 2700 rpm for five minutes, which was finally followed by addition into 800 mL of NSO (warmed to 40°C) with continuous stirring until two immiscible layers of biodiesel (top layer) and glycerol (bottom layer) were formed. This reaction was performed in 2000 mL conical flask and took 53 min. The conical flask was covered with aluminium foil and temperature was monitored by a thermometer under a constant temperature of 60°C; above this temperature, methanol will be boiled which will reduce the production of biodiesel [21]. The experiment was carried in a water bath until two immiscible layers of biodiesel (top layer) and glycerol (bottom layer) were formed [22]. This transesterification reaction takes place in alcoholic condition (methanol) as the media for the reaction to take place in presence of catalyst which speeds up the reaction but remains unchanged at the end of the reaction [23]. Both separating funnel and filtration methods were employed to isolate the catalyst from the reaction mixture and finally, the filtrate was washed and dried with anhydrous sodium sulphate [24]. The process was repeated using the same filtrate catalyst up to the fifth run. The transesterification process was repeated by varying catalyst dosage from 1 to 1.7 wt% and methanol-to-oil molar ratio varies from 2 : 1 to 16. Finally, biodiesel produced was tested using phenolphthalein indicator where the colour changes from clear to pink at a pH of 8-9 and the universal indicator was also used where the colour changes from green to dark green at pH of 8-9. However, the percentage of biodiesel yield was calculated by weighing the mass of biodiesel produced over the mass of oil used times hundred [25]. This was calculated using(1)percentage biodiesel yield=weight of biodiesel obtainedweight of oil used×100.


## 2.7. Characterization of Biodiesel Properties

Fatty acid composition analysis for NSO was done using Gas Chromatography-Mass Spectrometry (GC-MS), Anton Paar Stabinger viscometer SVM 4001, and density meter DMI 5000. Anton Paar.com instruments were used to determine kinematic viscosity at 40°C and density of biodiesel at 15.5°C per ASTM D7042 standards. Pour point and cloud point were determined by test cabinet instruments, PSL Systemtechnik/product/pour point tester 45150 and ASTM D2500 cloud point testing. The flashpoint was determined with the aid of Pensky-Martens flash point tester, PMA 5, Anton-Paar.com instruments as per ASTM D93 standards. The approximation of various values of acid, iodine, and saponification was done through the titration method.


## 2.8. Recyclability of the Catalyst

Heterogeneous catalysts have gained fame as compared to homogeneous catalysts because of their reusability [26]. Therefore, the recyclability of the catalyst synthesized in this study was determined as follows. Methanol was used to wash the catalyst spent in the biodiesel production to remove the contents of glycerol and oil. Since water is a product of the transesterification process, the catalyst was later oven-dried for 2 h at a temperature of 110°C. After drying and cooling, the spent catalyst was successfully used to produce biodiesel for the next successive run. Biodiesel yield produced was calculated after every successful run till the fifth run.


## 3. Results and Discussions

### 3.1. Characterization of the Catalyst

#### 3.1.1. Thermogravimetric Analysis (TGA)

Figure1 shows the TGA graph with plateaus at 650°C, a clear indication that all the impurities have been lost and mostly only the metal oxides such as CaO, K2CO3 MgO, and Na2O remained which increase the performance of the catalyst [27]. Above 740°C, most of the metal oxides like potassium were decomposed which decrease the basicity and, thus, decrease catalyst performance [28].Figure 1
Decomposition profile of catalyst between 29 and 800°.


#### 3.1.2. Textural Properties

For structural identification of CBA loaded with Li-CaO/Fe2(SO4)3 which was characterized, the BET method was used to determine the surface area, while Barret-Joyner Halenda (BJH) method was used to determine pore sizes and pore volume. CBA Li-CaO/Fe2(SO4)3 blends possess a BET surface of 411 m2/g, pore diameter of 3.0 nm, and pore volume of 0.628 cm3/g. According to previous studies on BET and BJH method in structural identification, CBA possesses a BET surface of 4 m2/g, pore diameter of 18 nm, and pore volume of 0.02 cm3/g (Betiku et al. [15]). According to Gohain et al. [16], CBA possesses a BET surface of 14 m2/g, pore diameter of 0.6 nm, and pore volume of 0.065 cm3/g. The CBA Li-CaO/Fe2(SO4)3 complex shows the large surface area as urged with results obtained by Zabeti et al. [29]. The CBA/Li-CaO/Fe2(SO4)3 contributed to an increase in performance and reusability of the catalyst due to its high basic contents with a pH of 11.1. This implies that specific surface area, as well as the pore volume, reusability, and high basic strength, may have a significant contribution to the performance of the catalyst.


#### 3.1.3. FT-IR Spectra Analysis

FT-IR spectra of banana ashes loaded with metal oxide Li-CaO/Fe2(SO4)3 were characterized as illustrated in Figures 2(a)–2(c) and compared to each other. The broadband at 3303 cm−1 in Figure 2(a) shows the stretching vibration of the O-H group and in Figures 2(b) and 2(c), the O-H group disappeared due to burning in air and calcination at 650°C. The sharp peak and small peak observed at 2920 cm−1 in Figure 2(a) and 2900–3150 cm−1 in Figures 2(b) and 2(c), respectively, show the stretching vibration of the C-H. Bands observed at 1350–1380 cm−1 have been associated with stretching vibrations of C-O from carbonate which show similarity with wavenumber [30]. The bending vibrations observed at 500–1020 cm−1 show some elements of interest since the peaks are associated with CaMgSiO4, Li2O, and FeSO4. It is worth mentioning that a well-pronounced peak of K2CO3 located at 1376 cm−1 is of special interest given that K2CO3 comes with several advantages such as increased catalyst performance, surface area, and reusability and prevents leaching as reported elsewhere [15].Figure 2
FT-IR peaks of banana ashes blends: (a) fresh banana ash blends, (b) burnt banana ash blends, and (c) calcined banana as blends.
(a)(b)(c)


#### 3.1.4. Morphological Analysis

A scanning electron microscope displays images at a magnification of 5000× resolution. The micrographs are shown in Figures3(a)–3(c) which represent fresh banana ash blends, burnt banana ash blends, and calcined banana ash blends. The surface of Figure 3(a) shows a smooth and flat nature of fresh banana ash blends, while Figure 3(b) has a mixture of small flake-like aggregates, and lastly Figure 3(c) displays interestingly sponge-like microstructure, a clear indicator of increased surface area which is proportional to the activity of the catalyst. This is in line with the argument of Sharma and his group who observed that heat treatment hinders leaching of K and, therefore, increases the life of the catalyst [31].Figure 3
SEM images of (a) fresh banana ash blends, (b) burnt banana ash blends, and (c) calcined banana ash blends.
(a)(b)(c)


#### 3.1.5. XRD Analysis

For crystallographic identification, XRD analysis was carried out on calcined banana ash (CBA) blends, burnt banana ash (BBA) blends, and fresh banana ash (FBA) blends as shown in Figures4(a)–4(c). There was a significant increase in potassium compounds with an increase in calcination temperature up to 650°C as shown in Figure 3(a). Sharp pronounced peaks at 2θ : 29 degrees correspond to K2CO3, whereas peaks at 2θ : 33 and 43 degrees correspond to CaMgSiO4 and KNaSO4, respectively. Remarkable crystallinity of the materials can be observed from the fact that the peaks are narrow with high intensity. Additionally, weak unmarked peaks in Figures 3(a)–3(c) may be attributed to trace elements like Fe2(SO4)3 and Li2O which have been reported to have a significant contribution to basicity and consequently optimize the catalyst performance (Betiku et al. [32]).Figure 4
XRD pattern of (a) calcined banana ash blends, (b) burnt banana ash blends, and (c) fresh banana ash blends.
(a)(b)(c)


#### 3.1.6. Elemental Composition of CBA

Table1 shows that the results of the XRF analysis carried on banana ashes calcined at different temperatures ranged from 550 to 1050°C and finally loaded with Li-CaO/Fe2(SO4)3. These results show the elemental composition present in banana ash. Main elements present in banana ash complex after sample analysis were K, Na, Ca, Mg, Fe, Al, Si, S, Li, and Cl. Potassium is the element of interest which has shown highest percentage (74.4%) composition after calcination at 650°C; the ash produced at 650°C was used as a catalyst for rapid production of biodiesel.Table 1
Elemental composition of CBA blends.
Temp (°C)KClSi (wt.%)NaSLiAlMgCaFe55054.657.374.9553.213.151.841.491.421.270.1465074.4110.885.222.880.002.960.211.191.620.2575072.5111.365.793.790.003.020.180.701.680.2885072.347.09.533.860.002.941.510.411.210.3595063.083.1920.343.330.0572.271.881.402.390.83105067.060.9216.154.490.393.171.111.553.220.642.2. Physicochemical Properties of NSOThe physicochemical results were shown in Table2. The amount of oil in one kilogram of neem seeds was 37.28% which was enough for the high production of biodiesel. From the following results, the concentration of acid value was reasonably high, suggesting that there was a high level of free fatty acid contents that probably would result in soap formation [11]. For oils with FFA contents higher than 1.1%, it is desirable to apply a biomass catalyst to maximize the yield of biodiesel production as this may prevent the reaction that results in soap formation [33]. The physicochemical identification of NSO like acid value and saponification value as well as iodine value was done through titration process in line with the agreements of American Society for Testing and Materials (ASTM) in the year 1983 and recommended the practice of official methods of American Oil Chemists Society (AOCS) [34].Table 2
Physicochemical properties of NSO.
PropertyUnitNSOOil content%37.28Acid valuemgKOH/g0.46Iodine valuegI2/100 g81.06Saponification valuemgKOH/g134.8Free fatty acid (FFA)mgKOH/g0.23The weight of oil extracted from a given mass in grams of seed pressed was measured to determine the lipid contents. The results were expressed as the percentage of oil in the dry matter [35]:(2)percentage of oil in sample=weight of dry seed−weight of residueweight of seed after dry.The acid value (AV) of neem oil was determined by titration method, diethyl ether, ethanol (95%), and phenolphthalein indicator, and a given mass oil sample in the mixture was titrated with 0.1 M NaOH in triplicate of experiments. The AV was calculated using the following equation [36]:(3)acid value=titre volume×grams of NaOH in 0.1M of NaOH solutionsample weight in grams.Iodine value (IV) is the measure of the degree of unsaturation of an oil or fat. Determination of IV in neem seed oil was carried out using laboratory titration method where a given mass of dry soil sample was mixed with a given volume of carbon tetrachloride, Wijis reagent 10%, potassium iodide solution, and distilled water to make a solution and titrate with 0.1 N of (Na2S2O3) sodium thiosulphate solution. The iodine value for the oil in the solution is calculated using the following equation [21]:(4)I.V=b−a×mass of iodine in 0.1N of sodium thiosulphatesample weight in grams,where a and b are average titration volumes (ml) of blank and oil solution and N is the normality of sodium thiosulphate.The saponification value (SV) of neem seed oil was determined by titrating a given mass of oil dissolved in a given volume of ethanolic potassium hydroxide (0.5 M in 95% ethanol) heated for one hour and then phenolphthalein indicator was added to the sample and then titrated with 0.5 MHCl. The saponification value was calculated using the following equation [37]:(5)S.V=b−a×grams of KOH in 0.5M KOH solutionsample weight in grams,where a indicates volume of oil solution and b indicates volume of titre of the blank solution [38]. One has(6)free fat acid=acid value2.


#### 3.1.7. Fatty Acid Profile of Neem Oil

Table3 shows that neem oil was extremely unsaturated (67.62%) due to the availability of linoleic acid, pentadecanoic acid, oleic acid, and linolenic acid as the major methyl esters. Literature reports that methyl esters from neem oil are extremely unsaturated [39].Table 3
Fatty acid composition of neem oil.
Fatty acidFormulaSystematic nameStructurewt.(%)Saturated fatty acidsPalmiticC16H32O2Hexadecanoic acid16 : 010.92StearicC18H36O2(E)-9-Octadecenoic acid18 : 119.85ArachidicC20H40O2Eicosanoic acid20.01.35LignocericC24H48O2Tetracosanoic acid24.00.26Total32.38Unsaturated fatty acidsPentadecanoicC17H34O2Pentadecanoic acid, 1417 : 12.57OleicC18H34O29-Octadecenoic acid18 : 11.82LinoleicC18H32O2:9,12-Octadecadienoic acid18 : 152.51LinolenicC18H30O29,12-Octadecatrienoic acid18 : 110.71Total67.62


### 3.2. Characterization of Biodiesel

The properties of biodiesel produced from blends of CBA/Li-CaO/Fe2 (SO4)3 are summarized in Table 4. Interestingly, these properties show similarities with the standards specified in EN 14214 and ASTM D 6751. For instance, the close similarity in cloud pour points, viscosity, initial boiling points, final boiling points, and acid value was observed. With an exception of density which was slightly higher than the recommended range, all other properties were per the ASTM D6751 standards. However, this biodiesel produced displayed remarkable cold flow properties like cloud point, pour point, and kinematic viscosity and may be used in cold areas. Also, the calorific value was high. It has been reported in the literature that both the molecular mass of methyl ester and its saturation level determine the density of biofuel; in short, the unsaturation level is directly proportional to the specific gravity [40]. The high density of biodiesel from neem oil may be due to the high unsaturation level. It is important to note that partial combustion has been reported because of the poor atomization process from the fact that denser fuels are less compressible [11]. Flashpoint as one of the most important parameters in the diesel engine can be defined as a minimum temperature at which fuel ignites [20]. In this study, it was about 150 °C. This temperature not only meets the required ASTM D6751 standards, which recommends a minimum of 130 °C, but also guarantees safety especially during storage and transportation [41]. The produced biodiesel and catalyst from this study show high yield compared to other studies as reported in Table 4.Table 4
Physicochemical properties of neem biodiesel.
Test/characteristicsPetrol diesel ASTM D975 limitsBiodiesel ASTM D 6751 limitsBiodieselDensity at 15 kg/m3850860–900863.8Kinematics viscosity at 40°C (mm2/s)2–4.51.9–6.03.8Pour point (°C)−35 to −15NS−30Flashpoint (°C)60–80130 min150Cloud point (°C)−15 to −5NS−40Cetane index (minimum)—4748.9Initial boiling point (°C)—NS86Final boiling point (°C)—NS86Calorific value42–46—43Acid value (titration) (mgKOH/g)—0.5 max0.12Table5 shows several precursors including but not limited to banana peels that have been investigated as biomass precursors for biodiesel production. For instance, Betiku et al. [15] researched on banana peel using Napoleon’s plumule oil and produced biodiesel 98.5% for 69-minute reaction time. In a similar study conducted by Gohain et al. [16], banana peel as a catalyst was used alongside waste cooking oil and it produces a biodiesel 96.3% for 60-minute reaction time. This study now reveals that CBA/Li-CaO/Fe2 (SO4)3 blended catalyst is anticipated to reduce the reaction time in the production of biodiesel 98.8% for 53-minute reaction time. Therefore, the blended catalyst is economical for the production of biodiesel from NSO as a possible alternative fuel feedstock in biodiesel production.Table 5
Comparison of the different performance of catalyst for biodiesel production.
Heterogeneous catalyst typeFeedstockSurface area (m2/g)Catalyst dosage (wt.%)Alcohol/oil ratioTemp (°C)Time (min)Yield (wt.%)ReferenceBanana peelsNapoleon’s plumule oil4.442.7530 : 16569.0298.50[15]Banana peelsWaste cooking oil14.03629 : 1608096.3[16]CBANeem seed oil411.21.78.1605398.80This study


### 3.3. Performance of Catalyst for Biodiesel Production

#### 3.3.1. The Effect of Catalyst Loading

The production of biodiesel yield was done by evaluating the percentage performance of the CBA blended catalyst using (1), by changing the conditions of the parameters of the reaction like percentage by weight of the catalyst added, the reaction time-temperature set, and the ratio of methanol and neem oil used. The amount of produced biodiesel was affected by the amount of the catalyst. The excess ratio of 16 : 1 of methanol to oil was used during testing the performance of the catalyst. The amount of catalyst added varied with the amount of oil at an interval of 0.1 wt% from 1 to 2 wt%. The effect of catalyst loaded on the rate of production of biodiesel yield was increased from 1.1 to 1.7 wt%, respectively, whereby the percentage of conversion of biodiesel was increased. The highest production yields 98.8% of biodiesel were attained at catalyst to oil weight of 1.7 wt% as shown in Figure 5. Several factors might have contributed to the high production yield of biodiesel, for example, the high surface area of the catalyst and presence of basic metal oxides such as K, Na, Ca, and Mg, which contributed to high basic strength 11.1 of the catalyst. Also, the availability of higher oxygen compounds in Li-CaO/Fe2(SO4)3 increases the rate of conversion methyl ester to biodiesel [42, 43].Figure 5
Effect of the amount of catalyst added on the production of biodiesel.


#### 3.3.2. Effect of Reaction Time

Production of biodiesel increases with the increase of time of the reaction [44]. The conversion rate of biodiesel depends on the time response for the required chemical reaction to take place [45]. The production biodiesel using NSO with 1.7 wt% catalyst loading and 8 : 1 excess methanol was done by changing the time of the reaction after every 10 min from 10 to 70 min while stirring at 2700 rpm and maintaining the temperature at 60°C. Figure 6 shows the effects of time on biodiesel yield. It is observed that the rate of production of biodiesel yield increases with time from 10 min to around 50 min. Above 50 min, biodiesel yield remained constant. This is due to a reversible reaction caused by the reduced and disappearance of esters resulting in soap formation associated with the fatty acid composition [46]. It observed that the proper time for the production of the highest yield of biodiesel is 53 min.Figure 6
Effect of reaction time on biodiesel yield.


#### 3.3.3. The Effect of Methanol-to-Oil Ratio

Key factors for converting long fatty acid esters to methyl esters (biodiesel) are the ratio of methanol to oil. The relation between quantities of substance and the number of moles that can take part in a chemical reaction is needed in the process [33]. This can result in the split of the mixture of reaction on the solubility of glycerol to the methyl ester layer. Figure 7 shows that the best ratio that can be seen as methanol-to-oil ratio of 8 : 1 highest yield of biodiesel was attained. This intensifies the equilibrium reaction which may affect the production biodiesel yield [46].Figure 7
Effect of the ratio of methanol and oil on a yield of biodiesel.


### 3.4. Catalyst Recyclability

Bio-based catalyst precursor prepared was reused up to the fifth run in the transesterification process, under the optimum condition, 1.7 wt% catalyst feed, methanol-to-oil molar ratio 8 : 1, 53 min time of the reaction, 60°C temperatures of the reaction, and stirring rate of 2700 rpm. From Figure8, one can see that catalyst performance in biodiesel yield decreased in every successive route. The yield was as follows: 98.8, 96.7, 85.7, 82.8, and 75.6% in the first, second, third, fourth, and fifth run, respectively. This may be due to the loss of functional groups of the catalyst. The loss of the catalyst active site may be due to H2O and CO2 from the environments. Recyclability of the catalyst numerously shows the great significance of the bio-based catalyst in minimizing waste disposal and production expenses and is environmentally friendly during the production of biodiesel.Figure 8
The recyclability catalyst versus % of biodiesel production.


## 3.1. Characterization of the Catalyst

### 3.1.1. Thermogravimetric Analysis (TGA)

Figure1 shows the TGA graph with plateaus at 650°C, a clear indication that all the impurities have been lost and mostly only the metal oxides such as CaO, K2CO3 MgO, and Na2O remained which increase the performance of the catalyst [27]. Above 740°C, most of the metal oxides like potassium were decomposed which decrease the basicity and, thus, decrease catalyst performance [28].Figure 1
Decomposition profile of catalyst between 29 and 800°.


### 3.1.2. Textural Properties

For structural identification of CBA loaded with Li-CaO/Fe2(SO4)3 which was characterized, the BET method was used to determine the surface area, while Barret-Joyner Halenda (BJH) method was used to determine pore sizes and pore volume. CBA Li-CaO/Fe2(SO4)3 blends possess a BET surface of 411 m2/g, pore diameter of 3.0 nm, and pore volume of 0.628 cm3/g. According to previous studies on BET and BJH method in structural identification, CBA possesses a BET surface of 4 m2/g, pore diameter of 18 nm, and pore volume of 0.02 cm3/g (Betiku et al. [15]). According to Gohain et al. [16], CBA possesses a BET surface of 14 m2/g, pore diameter of 0.6 nm, and pore volume of 0.065 cm3/g. The CBA Li-CaO/Fe2(SO4)3 complex shows the large surface area as urged with results obtained by Zabeti et al. [29]. The CBA/Li-CaO/Fe2(SO4)3 contributed to an increase in performance and reusability of the catalyst due to its high basic contents with a pH of 11.1. This implies that specific surface area, as well as the pore volume, reusability, and high basic strength, may have a significant contribution to the performance of the catalyst.


### 3.1.3. FT-IR Spectra Analysis

FT-IR spectra of banana ashes loaded with metal oxide Li-CaO/Fe2(SO4)3 were characterized as illustrated in Figures 2(a)–2(c) and compared to each other. The broadband at 3303 cm−1 in Figure 2(a) shows the stretching vibration of the O-H group and in Figures 2(b) and 2(c), the O-H group disappeared due to burning in air and calcination at 650°C. The sharp peak and small peak observed at 2920 cm−1 in Figure 2(a) and 2900–3150 cm−1 in Figures 2(b) and 2(c), respectively, show the stretching vibration of the C-H. Bands observed at 1350–1380 cm−1 have been associated with stretching vibrations of C-O from carbonate which show similarity with wavenumber [30]. The bending vibrations observed at 500–1020 cm−1 show some elements of interest since the peaks are associated with CaMgSiO4, Li2O, and FeSO4. It is worth mentioning that a well-pronounced peak of K2CO3 located at 1376 cm−1 is of special interest given that K2CO3 comes with several advantages such as increased catalyst performance, surface area, and reusability and prevents leaching as reported elsewhere [15].Figure 2
FT-IR peaks of banana ashes blends: (a) fresh banana ash blends, (b) burnt banana ash blends, and (c) calcined banana as blends.
(a)(b)(c)


### 3.1.4. Morphological Analysis

A scanning electron microscope displays images at a magnification of 5000× resolution. The micrographs are shown in Figures3(a)–3(c) which represent fresh banana ash blends, burnt banana ash blends, and calcined banana ash blends. The surface of Figure 3(a) shows a smooth and flat nature of fresh banana ash blends, while Figure 3(b) has a mixture of small flake-like aggregates, and lastly Figure 3(c) displays interestingly sponge-like microstructure, a clear indicator of increased surface area which is proportional to the activity of the catalyst. This is in line with the argument of Sharma and his group who observed that heat treatment hinders leaching of K and, therefore, increases the life of the catalyst [31].Figure 3
SEM images of (a) fresh banana ash blends, (b) burnt banana ash blends, and (c) calcined banana ash blends.
(a)(b)(c)


### 3.1.5. XRD Analysis

For crystallographic identification, XRD analysis was carried out on calcined banana ash (CBA) blends, burnt banana ash (BBA) blends, and fresh banana ash (FBA) blends as shown in Figures4(a)–4(c). There was a significant increase in potassium compounds with an increase in calcination temperature up to 650°C as shown in Figure 3(a). Sharp pronounced peaks at 2θ : 29 degrees correspond to K2CO3, whereas peaks at 2θ : 33 and 43 degrees correspond to CaMgSiO4 and KNaSO4, respectively. Remarkable crystallinity of the materials can be observed from the fact that the peaks are narrow with high intensity. Additionally, weak unmarked peaks in Figures 3(a)–3(c) may be attributed to trace elements like Fe2(SO4)3 and Li2O which have been reported to have a significant contribution to basicity and consequently optimize the catalyst performance (Betiku et al. [32]).Figure 4
XRD pattern of (a) calcined banana ash blends, (b) burnt banana ash blends, and (c) fresh banana ash blends.
(a)(b)(c)


### 3.1.6. Elemental Composition of CBA

Table1 shows that the results of the XRF analysis carried on banana ashes calcined at different temperatures ranged from 550 to 1050°C and finally loaded with Li-CaO/Fe2(SO4)3. These results show the elemental composition present in banana ash. Main elements present in banana ash complex after sample analysis were K, Na, Ca, Mg, Fe, Al, Si, S, Li, and Cl. Potassium is the element of interest which has shown highest percentage (74.4%) composition after calcination at 650°C; the ash produced at 650°C was used as a catalyst for rapid production of biodiesel.Table 1
Elemental composition of CBA blends.
Temp (°C)KClSi (wt.%)NaSLiAlMgCaFe55054.657.374.9553.213.151.841.491.421.270.1465074.4110.885.222.880.002.960.211.191.620.2575072.5111.365.793.790.003.020.180.701.680.2885072.347.09.533.860.002.941.510.411.210.3595063.083.1920.343.330.0572.271.881.402.390.83105067.060.9216.154.490.393.171.111.553.220.642.2. Physicochemical Properties of NSOThe physicochemical results were shown in Table2. The amount of oil in one kilogram of neem seeds was 37.28% which was enough for the high production of biodiesel. From the following results, the concentration of acid value was reasonably high, suggesting that there was a high level of free fatty acid contents that probably would result in soap formation [11]. For oils with FFA contents higher than 1.1%, it is desirable to apply a biomass catalyst to maximize the yield of biodiesel production as this may prevent the reaction that results in soap formation [33]. The physicochemical identification of NSO like acid value and saponification value as well as iodine value was done through titration process in line with the agreements of American Society for Testing and Materials (ASTM) in the year 1983 and recommended the practice of official methods of American Oil Chemists Society (AOCS) [34].Table 2
Physicochemical properties of NSO.
PropertyUnitNSOOil content%37.28Acid valuemgKOH/g0.46Iodine valuegI2/100 g81.06Saponification valuemgKOH/g134.8Free fatty acid (FFA)mgKOH/g0.23The weight of oil extracted from a given mass in grams of seed pressed was measured to determine the lipid contents. The results were expressed as the percentage of oil in the dry matter [35]:(2)percentage of oil in sample=weight of dry seed−weight of residueweight of seed after dry.The acid value (AV) of neem oil was determined by titration method, diethyl ether, ethanol (95%), and phenolphthalein indicator, and a given mass oil sample in the mixture was titrated with 0.1 M NaOH in triplicate of experiments. The AV was calculated using the following equation [36]:(3)acid value=titre volume×grams of NaOH in 0.1M of NaOH solutionsample weight in grams.Iodine value (IV) is the measure of the degree of unsaturation of an oil or fat. Determination of IV in neem seed oil was carried out using laboratory titration method where a given mass of dry soil sample was mixed with a given volume of carbon tetrachloride, Wijis reagent 10%, potassium iodide solution, and distilled water to make a solution and titrate with 0.1 N of (Na2S2O3) sodium thiosulphate solution. The iodine value for the oil in the solution is calculated using the following equation [21]:(4)I.V=b−a×mass of iodine in 0.1N of sodium thiosulphatesample weight in grams,where a and b are average titration volumes (ml) of blank and oil solution and N is the normality of sodium thiosulphate.The saponification value (SV) of neem seed oil was determined by titrating a given mass of oil dissolved in a given volume of ethanolic potassium hydroxide (0.5 M in 95% ethanol) heated for one hour and then phenolphthalein indicator was added to the sample and then titrated with 0.5 MHCl. The saponification value was calculated using the following equation [37]:(5)S.V=b−a×grams of KOH in 0.5M KOH solutionsample weight in grams,where a indicates volume of oil solution and b indicates volume of titre of the blank solution [38]. One has(6)free fat acid=acid value2.


### 3.1.7. Fatty Acid Profile of Neem Oil

Table3 shows that neem oil was extremely unsaturated (67.62%) due to the availability of linoleic acid, pentadecanoic acid, oleic acid, and linolenic acid as the major methyl esters. Literature reports that methyl esters from neem oil are extremely unsaturated [39].Table 3
Fatty acid composition of neem oil.
Fatty acidFormulaSystematic nameStructurewt.(%)Saturated fatty acidsPalmiticC16H32O2Hexadecanoic acid16 : 010.92StearicC18H36O2(E)-9-Octadecenoic acid18 : 119.85ArachidicC20H40O2Eicosanoic acid20.01.35LignocericC24H48O2Tetracosanoic acid24.00.26Total32.38Unsaturated fatty acidsPentadecanoicC17H34O2Pentadecanoic acid, 1417 : 12.57OleicC18H34O29-Octadecenoic acid18 : 11.82LinoleicC18H32O2:9,12-Octadecadienoic acid18 : 152.51LinolenicC18H30O29,12-Octadecatrienoic acid18 : 110.71Total67.62


## 3.1.1. Thermogravimetric Analysis (TGA)

Figure1 shows the TGA graph with plateaus at 650°C, a clear indication that all the impurities have been lost and mostly only the metal oxides such as CaO, K2CO3 MgO, and Na2O remained which increase the performance of the catalyst [27]. Above 740°C, most of the metal oxides like potassium were decomposed which decrease the basicity and, thus, decrease catalyst performance [28].Figure 1
Decomposition profile of catalyst between 29 and 800°.


## 3.1.2. Textural Properties

For structural identification of CBA loaded with Li-CaO/Fe2(SO4)3 which was characterized, the BET method was used to determine the surface area, while Barret-Joyner Halenda (BJH) method was used to determine pore sizes and pore volume. CBA Li-CaO/Fe2(SO4)3 blends possess a BET surface of 411 m2/g, pore diameter of 3.0 nm, and pore volume of 0.628 cm3/g. According to previous studies on BET and BJH method in structural identification, CBA possesses a BET surface of 4 m2/g, pore diameter of 18 nm, and pore volume of 0.02 cm3/g (Betiku et al. [15]). According to Gohain et al. [16], CBA possesses a BET surface of 14 m2/g, pore diameter of 0.6 nm, and pore volume of 0.065 cm3/g. The CBA Li-CaO/Fe2(SO4)3 complex shows the large surface area as urged with results obtained by Zabeti et al. [29]. The CBA/Li-CaO/Fe2(SO4)3 contributed to an increase in performance and reusability of the catalyst due to its high basic contents with a pH of 11.1. This implies that specific surface area, as well as the pore volume, reusability, and high basic strength, may have a significant contribution to the performance of the catalyst.


## 3.1.3. FT-IR Spectra Analysis

FT-IR spectra of banana ashes loaded with metal oxide Li-CaO/Fe2(SO4)3 were characterized as illustrated in Figures 2(a)–2(c) and compared to each other. The broadband at 3303 cm−1 in Figure 2(a) shows the stretching vibration of the O-H group and in Figures 2(b) and 2(c), the O-H group disappeared due to burning in air and calcination at 650°C. The sharp peak and small peak observed at 2920 cm−1 in Figure 2(a) and 2900–3150 cm−1 in Figures 2(b) and 2(c), respectively, show the stretching vibration of the C-H. Bands observed at 1350–1380 cm−1 have been associated with stretching vibrations of C-O from carbonate which show similarity with wavenumber [30]. The bending vibrations observed at 500–1020 cm−1 show some elements of interest since the peaks are associated with CaMgSiO4, Li2O, and FeSO4. It is worth mentioning that a well-pronounced peak of K2CO3 located at 1376 cm−1 is of special interest given that K2CO3 comes with several advantages such as increased catalyst performance, surface area, and reusability and prevents leaching as reported elsewhere [15].Figure 2
FT-IR peaks of banana ashes blends: (a) fresh banana ash blends, (b) burnt banana ash blends, and (c) calcined banana as blends.
(a)(b)(c)


## 3.1.4. Morphological Analysis

A scanning electron microscope displays images at a magnification of 5000× resolution. The micrographs are shown in Figures3(a)–3(c) which represent fresh banana ash blends, burnt banana ash blends, and calcined banana ash blends. The surface of Figure 3(a) shows a smooth and flat nature of fresh banana ash blends, while Figure 3(b) has a mixture of small flake-like aggregates, and lastly Figure 3(c) displays interestingly sponge-like microstructure, a clear indicator of increased surface area which is proportional to the activity of the catalyst. This is in line with the argument of Sharma and his group who observed that heat treatment hinders leaching of K and, therefore, increases the life of the catalyst [31].Figure 3
SEM images of (a) fresh banana ash blends, (b) burnt banana ash blends, and (c) calcined banana ash blends.
(a)(b)(c)


## 3.1.5. XRD Analysis

For crystallographic identification, XRD analysis was carried out on calcined banana ash (CBA) blends, burnt banana ash (BBA) blends, and fresh banana ash (FBA) blends as shown in Figures4(a)–4(c). There was a significant increase in potassium compounds with an increase in calcination temperature up to 650°C as shown in Figure 3(a). Sharp pronounced peaks at 2θ : 29 degrees correspond to K2CO3, whereas peaks at 2θ : 33 and 43 degrees correspond to CaMgSiO4 and KNaSO4, respectively. Remarkable crystallinity of the materials can be observed from the fact that the peaks are narrow with high intensity. Additionally, weak unmarked peaks in Figures 3(a)–3(c) may be attributed to trace elements like Fe2(SO4)3 and Li2O which have been reported to have a significant contribution to basicity and consequently optimize the catalyst performance (Betiku et al. [32]).Figure 4
XRD pattern of (a) calcined banana ash blends, (b) burnt banana ash blends, and (c) fresh banana ash blends.
(a)(b)(c)


## 3.1.6. Elemental Composition of CBA

Table1 shows that the results of the XRF analysis carried on banana ashes calcined at different temperatures ranged from 550 to 1050°C and finally loaded with Li-CaO/Fe2(SO4)3. These results show the elemental composition present in banana ash. Main elements present in banana ash complex after sample analysis were K, Na, Ca, Mg, Fe, Al, Si, S, Li, and Cl. Potassium is the element of interest which has shown highest percentage (74.4%) composition after calcination at 650°C; the ash produced at 650°C was used as a catalyst for rapid production of biodiesel.Table 1
Elemental composition of CBA blends.
Temp (°C)KClSi (wt.%)NaSLiAlMgCaFe55054.657.374.9553.213.151.841.491.421.270.1465074.4110.885.222.880.002.960.211.191.620.2575072.5111.365.793.790.003.020.180.701.680.2885072.347.09.533.860.002.941.510.411.210.3595063.083.1920.343.330.0572.271.881.402.390.83105067.060.9216.154.490.393.171.111.553.220.642.2. Physicochemical Properties of NSOThe physicochemical results were shown in Table2. The amount of oil in one kilogram of neem seeds was 37.28% which was enough for the high production of biodiesel. From the following results, the concentration of acid value was reasonably high, suggesting that there was a high level of free fatty acid contents that probably would result in soap formation [11]. For oils with FFA contents higher than 1.1%, it is desirable to apply a biomass catalyst to maximize the yield of biodiesel production as this may prevent the reaction that results in soap formation [33]. The physicochemical identification of NSO like acid value and saponification value as well as iodine value was done through titration process in line with the agreements of American Society for Testing and Materials (ASTM) in the year 1983 and recommended the practice of official methods of American Oil Chemists Society (AOCS) [34].Table 2
Physicochemical properties of NSO.
PropertyUnitNSOOil content%37.28Acid valuemgKOH/g0.46Iodine valuegI2/100 g81.06Saponification valuemgKOH/g134.8Free fatty acid (FFA)mgKOH/g0.23The weight of oil extracted from a given mass in grams of seed pressed was measured to determine the lipid contents. The results were expressed as the percentage of oil in the dry matter [35]:(2)percentage of oil in sample=weight of dry seed−weight of residueweight of seed after dry.The acid value (AV) of neem oil was determined by titration method, diethyl ether, ethanol (95%), and phenolphthalein indicator, and a given mass oil sample in the mixture was titrated with 0.1 M NaOH in triplicate of experiments. The AV was calculated using the following equation [36]:(3)acid value=titre volume×grams of NaOH in 0.1M of NaOH solutionsample weight in grams.Iodine value (IV) is the measure of the degree of unsaturation of an oil or fat. Determination of IV in neem seed oil was carried out using laboratory titration method where a given mass of dry soil sample was mixed with a given volume of carbon tetrachloride, Wijis reagent 10%, potassium iodide solution, and distilled water to make a solution and titrate with 0.1 N of (Na2S2O3) sodium thiosulphate solution. The iodine value for the oil in the solution is calculated using the following equation [21]:(4)I.V=b−a×mass of iodine in 0.1N of sodium thiosulphatesample weight in grams,where a and b are average titration volumes (ml) of blank and oil solution and N is the normality of sodium thiosulphate.The saponification value (SV) of neem seed oil was determined by titrating a given mass of oil dissolved in a given volume of ethanolic potassium hydroxide (0.5 M in 95% ethanol) heated for one hour and then phenolphthalein indicator was added to the sample and then titrated with 0.5 MHCl. The saponification value was calculated using the following equation [37]:(5)S.V=b−a×grams of KOH in 0.5M KOH solutionsample weight in grams,where a indicates volume of oil solution and b indicates volume of titre of the blank solution [38]. One has(6)free fat acid=acid value2.


## 3.1.7. Fatty Acid Profile of Neem Oil

Table3 shows that neem oil was extremely unsaturated (67.62%) due to the availability of linoleic acid, pentadecanoic acid, oleic acid, and linolenic acid as the major methyl esters. Literature reports that methyl esters from neem oil are extremely unsaturated [39].Table 3
Fatty acid composition of neem oil.
Fatty acidFormulaSystematic nameStructurewt.(%)Saturated fatty acidsPalmiticC16H32O2Hexadecanoic acid16 : 010.92StearicC18H36O2(E)-9-Octadecenoic acid18 : 119.85ArachidicC20H40O2Eicosanoic acid20.01.35LignocericC24H48O2Tetracosanoic acid24.00.26Total32.38Unsaturated fatty acidsPentadecanoicC17H34O2Pentadecanoic acid, 1417 : 12.57OleicC18H34O29-Octadecenoic acid18 : 11.82LinoleicC18H32O2:9,12-Octadecadienoic acid18 : 152.51LinolenicC18H30O29,12-Octadecatrienoic acid18 : 110.71Total67.62


## 3.2. Characterization of Biodiesel

The properties of biodiesel produced from blends of CBA/Li-CaO/Fe2 (SO4)3 are summarized in Table 4. Interestingly, these properties show similarities with the standards specified in EN 14214 and ASTM D 6751. For instance, the close similarity in cloud pour points, viscosity, initial boiling points, final boiling points, and acid value was observed. With an exception of density which was slightly higher than the recommended range, all other properties were per the ASTM D6751 standards. However, this biodiesel produced displayed remarkable cold flow properties like cloud point, pour point, and kinematic viscosity and may be used in cold areas. Also, the calorific value was high. It has been reported in the literature that both the molecular mass of methyl ester and its saturation level determine the density of biofuel; in short, the unsaturation level is directly proportional to the specific gravity [40]. The high density of biodiesel from neem oil may be due to the high unsaturation level. It is important to note that partial combustion has been reported because of the poor atomization process from the fact that denser fuels are less compressible [11]. Flashpoint as one of the most important parameters in the diesel engine can be defined as a minimum temperature at which fuel ignites [20]. In this study, it was about 150 °C. This temperature not only meets the required ASTM D6751 standards, which recommends a minimum of 130 °C, but also guarantees safety especially during storage and transportation [41]. The produced biodiesel and catalyst from this study show high yield compared to other studies as reported in Table 4.Table 4
Physicochemical properties of neem biodiesel.
Test/characteristicsPetrol diesel ASTM D975 limitsBiodiesel ASTM D 6751 limitsBiodieselDensity at 15 kg/m3850860–900863.8Kinematics viscosity at 40°C (mm2/s)2–4.51.9–6.03.8Pour point (°C)−35 to −15NS−30Flashpoint (°C)60–80130 min150Cloud point (°C)−15 to −5NS−40Cetane index (minimum)—4748.9Initial boiling point (°C)—NS86Final boiling point (°C)—NS86Calorific value42–46—43Acid value (titration) (mgKOH/g)—0.5 max0.12Table5 shows several precursors including but not limited to banana peels that have been investigated as biomass precursors for biodiesel production. For instance, Betiku et al. [15] researched on banana peel using Napoleon’s plumule oil and produced biodiesel 98.5% for 69-minute reaction time. In a similar study conducted by Gohain et al. [16], banana peel as a catalyst was used alongside waste cooking oil and it produces a biodiesel 96.3% for 60-minute reaction time. This study now reveals that CBA/Li-CaO/Fe2 (SO4)3 blended catalyst is anticipated to reduce the reaction time in the production of biodiesel 98.8% for 53-minute reaction time. Therefore, the blended catalyst is economical for the production of biodiesel from NSO as a possible alternative fuel feedstock in biodiesel production.Table 5
Comparison of the different performance of catalyst for biodiesel production.
Heterogeneous catalyst typeFeedstockSurface area (m2/g)Catalyst dosage (wt.%)Alcohol/oil ratioTemp (°C)Time (min)Yield (wt.%)ReferenceBanana peelsNapoleon’s plumule oil4.442.7530 : 16569.0298.50[15]Banana peelsWaste cooking oil14.03629 : 1608096.3[16]CBANeem seed oil411.21.78.1605398.80This study


## 3.3. Performance of Catalyst for Biodiesel Production

### 3.3.1. The Effect of Catalyst Loading

The production of biodiesel yield was done by evaluating the percentage performance of the CBA blended catalyst using (1), by changing the conditions of the parameters of the reaction like percentage by weight of the catalyst added, the reaction time-temperature set, and the ratio of methanol and neem oil used. The amount of produced biodiesel was affected by the amount of the catalyst. The excess ratio of 16 : 1 of methanol to oil was used during testing the performance of the catalyst. The amount of catalyst added varied with the amount of oil at an interval of 0.1 wt% from 1 to 2 wt%. The effect of catalyst loaded on the rate of production of biodiesel yield was increased from 1.1 to 1.7 wt%, respectively, whereby the percentage of conversion of biodiesel was increased. The highest production yields 98.8% of biodiesel were attained at catalyst to oil weight of 1.7 wt% as shown in Figure 5. Several factors might have contributed to the high production yield of biodiesel, for example, the high surface area of the catalyst and presence of basic metal oxides such as K, Na, Ca, and Mg, which contributed to high basic strength 11.1 of the catalyst. Also, the availability of higher oxygen compounds in Li-CaO/Fe2(SO4)3 increases the rate of conversion methyl ester to biodiesel [42, 43].Figure 5
Effect of the amount of catalyst added on the production of biodiesel.


### 3.3.2. Effect of Reaction Time

Production of biodiesel increases with the increase of time of the reaction [44]. The conversion rate of biodiesel depends on the time response for the required chemical reaction to take place [45]. The production biodiesel using NSO with 1.7 wt% catalyst loading and 8 : 1 excess methanol was done by changing the time of the reaction after every 10 min from 10 to 70 min while stirring at 2700 rpm and maintaining the temperature at 60°C. Figure 6 shows the effects of time on biodiesel yield. It is observed that the rate of production of biodiesel yield increases with time from 10 min to around 50 min. Above 50 min, biodiesel yield remained constant. This is due to a reversible reaction caused by the reduced and disappearance of esters resulting in soap formation associated with the fatty acid composition [46]. It observed that the proper time for the production of the highest yield of biodiesel is 53 min.Figure 6
Effect of reaction time on biodiesel yield.


### 3.3.3. The Effect of Methanol-to-Oil Ratio

Key factors for converting long fatty acid esters to methyl esters (biodiesel) are the ratio of methanol to oil. The relation between quantities of substance and the number of moles that can take part in a chemical reaction is needed in the process [33]. This can result in the split of the mixture of reaction on the solubility of glycerol to the methyl ester layer. Figure 7 shows that the best ratio that can be seen as methanol-to-oil ratio of 8 : 1 highest yield of biodiesel was attained. This intensifies the equilibrium reaction which may affect the production biodiesel yield [46].Figure 7
Effect of the ratio of methanol and oil on a yield of biodiesel.


## 3.3.1. The Effect of Catalyst Loading

The production of biodiesel yield was done by evaluating the percentage performance of the CBA blended catalyst using (1), by changing the conditions of the parameters of the reaction like percentage by weight of the catalyst added, the reaction time-temperature set, and the ratio of methanol and neem oil used. The amount of produced biodiesel was affected by the amount of the catalyst. The excess ratio of 16 : 1 of methanol to oil was used during testing the performance of the catalyst. The amount of catalyst added varied with the amount of oil at an interval of 0.1 wt% from 1 to 2 wt%. The effect of catalyst loaded on the rate of production of biodiesel yield was increased from 1.1 to 1.7 wt%, respectively, whereby the percentage of conversion of biodiesel was increased. The highest production yields 98.8% of biodiesel were attained at catalyst to oil weight of 1.7 wt% as shown in Figure 5. Several factors might have contributed to the high production yield of biodiesel, for example, the high surface area of the catalyst and presence of basic metal oxides such as K, Na, Ca, and Mg, which contributed to high basic strength 11.1 of the catalyst. Also, the availability of higher oxygen compounds in Li-CaO/Fe2(SO4)3 increases the rate of conversion methyl ester to biodiesel [42, 43].Figure 5
Effect of the amount of catalyst added on the production of biodiesel.


## 3.3.2. Effect of Reaction Time

Production of biodiesel increases with the increase of time of the reaction [44]. The conversion rate of biodiesel depends on the time response for the required chemical reaction to take place [45]. The production biodiesel using NSO with 1.7 wt% catalyst loading and 8 : 1 excess methanol was done by changing the time of the reaction after every 10 min from 10 to 70 min while stirring at 2700 rpm and maintaining the temperature at 60°C. Figure 6 shows the effects of time on biodiesel yield. It is observed that the rate of production of biodiesel yield increases with time from 10 min to around 50 min. Above 50 min, biodiesel yield remained constant. This is due to a reversible reaction caused by the reduced and disappearance of esters resulting in soap formation associated with the fatty acid composition [46]. It observed that the proper time for the production of the highest yield of biodiesel is 53 min.Figure 6
Effect of reaction time on biodiesel yield.


## 3.3.3. The Effect of Methanol-to-Oil Ratio

Key factors for converting long fatty acid esters to methyl esters (biodiesel) are the ratio of methanol to oil. The relation between quantities of substance and the number of moles that can take part in a chemical reaction is needed in the process [33]. This can result in the split of the mixture of reaction on the solubility of glycerol to the methyl ester layer. Figure 7 shows that the best ratio that can be seen as methanol-to-oil ratio of 8 : 1 highest yield of biodiesel was attained. This intensifies the equilibrium reaction which may affect the production biodiesel yield [46].Figure 7
Effect of the ratio of methanol and oil on a yield of biodiesel.


## 3.4. Catalyst Recyclability

Bio-based catalyst precursor prepared was reused up to the fifth run in the transesterification process, under the optimum condition, 1.7 wt% catalyst feed, methanol-to-oil molar ratio 8 : 1, 53 min time of the reaction, 60°C temperatures of the reaction, and stirring rate of 2700 rpm. From Figure8, one can see that catalyst performance in biodiesel yield decreased in every successive route. The yield was as follows: 98.8, 96.7, 85.7, 82.8, and 75.6% in the first, second, third, fourth, and fifth run, respectively. This may be due to the loss of functional groups of the catalyst. The loss of the catalyst active site may be due to H2O and CO2 from the environments. Recyclability of the catalyst numerously shows the great significance of the bio-based catalyst in minimizing waste disposal and production expenses and is environmentally friendly during the production of biodiesel.Figure 8
The recyclability catalyst versus % of biodiesel production.


## 4. Conclusion

This study presents the production of biodiesel from NSO and affordable solid catalyst synthesized by direct calcination of banana peels. Calcined banana peels at 650°C acquired good catalytic activity due to the presence of basic metal oxides of K, Ca, Na, and Mg and basic strength of 11.09. The performance was also attributed to its high specific surface area of 411 m2/g and pore diameter of 3.0 nm. The maximum biodiesel production yield of 98.8% was achieved at a low catalyst loading of 1.7 wt% and 8 : 1 methanol-to-oil molar ratio at a temperature of 60°C. The produced biodiesel acquired physicochemical parameters within the recommended ASTM D6751 standards and it displayed remarkable cold flow properties, that is, cloud point, pour point, and kinematic viscosity, and may be used in cold areas; also the calorific value was high. The catalyst shows good reusability properties with a yield of approximately 75% after a fifth run. It can be concluded that the produced CBA catalyst minimizes waste disposal, hence standing out as an environmentally compatible catalyst.



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*Source: 7825024-2020-08-27.xml*