Catalyst and Elemental Analysis Involving Biodiesel from Various Feedstocks

: The world is currently faced with the depletion of fossil fuel energy sources and their use is associated with environmental pollution. This has triggered the need to seek alternative energy sources that are renewable, sustainable and environmentally benign. Biodiesel, an alternative fuel of interest, is obtainable from biomass feedstocks. In existing biodiesel fuel, there are concerns that it is a contaminant due to its elemental contents, which over time also affect its quality. This study aimed to investigate the inﬂuence of a bifunctional catalyst on the conversion of free fatty acids and the elemental composition of biodiesel obtained from waste oils of sunﬂower and palm feedstocks. The synthesised catalyst was characterised using BET, XRD, FTIR and SEM while ICP-OES and Rancimat were used for elemental contents and oxidation in feedstocks and biodiesels. The effect of Cu, Zn and Fe metals on the stability of synthesised biodiesel was further studied. The catalyst showed characteristics of bifunctionality with improved textural properties necessary for the conversion of high free fatty acids feedstocks to biodiesel, despite increasing Ca content within the produced biodiesel. Sunﬂower biodiesel showed superior fuel quality, although palm biodiesel had more oxidation stability. An increase in the concentration of metals decreased the induction period, with Cu and Fe being more effective than Zn metal. which was characterised using FTIR, SEM, XRD and BET. The catalyst was used in transesteriﬁcation biodiesel from waste cooking oils of palm and sunﬂower. Evaluation of the elemental contents from feedstocks to biodiesel produced was performed by ICP-OES and fuel properties were characterised by Density Meter, Flash Tester, Viscometer and FTIR spectrometer. Additionally, the effect of Cu, Zn and Fe on oxidation stability of the produced biodiesels was also studied.


Introduction
Global primary energy demand is set to experience an annual increase of 1.46% from 2009 to 2035 [1]. This is not surprising, as industrialisation has grown significantly with a rise in the global population to 7.3 billion in 2015, which is projected to further grow to 9.2 billion in 2040 [2]. The enormous use of fossil fuels has put the environment and human health at risk [3,4], with energy utilisation especially high in the transportation sector, which is expected to make up about 63% of total global fuel consumption from 2010 to 2040 [5,6].
In 2008, it was reported that the transportation sector contributed to about 23% of total CO 2 emissions globally [7,8], with 73% of this contribution made by road transport [9], while the contribution from fuel combustion increases by 1.6% per year [1]. This will lead to severe ecological impacts, namely air and noise pollution, an increase in global surface temperatures (excess of 6 • C), changes in rainfall patterns and subsequently extreme weather events [1,[10][11][12].
Apart from the potential exhaustion of petroleum reserves over time [13], fuel prices have increased [14] due to oil reserves being concentrated in specific regions in the world [15], giving rise to some political conflicts. Therefore, a more significant sustainable movement led by advancement towards environmental conservation, a feasible economy

Results
This section gives an overview of the bifunctional CaO/AI 2 O 3 catalyst synthesised using the wet impregnation method, as well as the characterisation of the synthesised catalyst using SEM, XRD, FTIR and BET to determine the surface morphology, crystalline structure, functional groups and surface area, pore volume and diameter. Also discussed in this section is the fatty acids content within each feedstock estimation and the fuel properties determined using the gas chromatography (GC), viscometer, density meter, flash tester, color-indicator titrator and FTIR.

Bifunctional Catalyst Characterisation
The FTIR spectrum of CaO, Al 2 O 3 and CaO/Al 2 O 3 catalyst is shown in Figure 1, with absorption bands in the range of 400-4000 cm −1 . Figure 1a shows all characteristic peaks of CaO with a broad CO 3 stretch at 1409.32 cm −1 and a smaller CaO band [45], while the presence of water molecules in the un-calcined catalyst was observed with a strong hydroxy (H-O) band appearing at 3640.79 cm −1 [46]. Intense peaks at 636.06 cm −1 , 554.55 cm −1 and 485.48 cm −1 are presented in Figure 1b, with dominancy of Al-O normally found in the region of 1000-400 cm −1 [47]. The synthesised CaO/Al 2 O 3 catalyst was confirmed by the co-existing of Ca-O and Al-O within the CaO/Al 2 O 3 catalyst as shown in Figure 1c, by the presence of CaO absorption bands at 875 cm −1 and 713 cm −1 correspondings to C-O and Ca-O bonding and by a broader CaCO 3 band at 1469.80 cm −1 . The H-bonded hydroxyl group appeared due to moisture and the presence of CO 2 [48]. Furthermore, Table 1 re-affirms these compositions within the synthesised catalyst.     The external morphological characteristics of Al 2 O 3 and synthesised CaO/Al 2 O 3 catalyst after calcination at 475 • C were studied by SEM. Figure 2a,b illustrates the morphology of commercial Al 2 O 3 particles appearing as crystals of corundum, normally found to promote densification of corundum shape-like composites which help in enhancing performance [49]. After thermal treatment with high temperatures for 5 h (hr) and impregnation of CaO, a modification of Al 2 O 3 into irregularly shaped clusters due to the breakage of large particles into smaller pieces [50], with the intensification of CaO particle agglomeration on the support, can be observed in Figure 2. This is due to the huge percentage of metal oxide which normally has an irregular shape even after thermal treatment [25], and the presence of impurities and unconverted Ca(OH) 2 [51]. Micrographs were in agreement with the results found in Table 2, where the supported oxide in Figure 2c,d showed the increased surface area and increased pore size distribution as was also reported by Young et al. [52], which increases activity due to the formation of more active sites on the surface area and has an effect on the reaction rates and selectivity [53].
Catalysts 2021, 11, x FOR PEER REVIEW 5 of 18 metal oxide which normally has an irregular shape even after thermal treatment [25], and the presence of impurities and unconverted Ca(OH)2 [51]. Micrographs were in agreement with the results found in Table 2, where the supported oxide in Figure 2c,d showed the increased surface area and increased pore size distribution as was also reported by Young et al. [52], which increases activity due to the formation of more active sites on the surface area and has an effect on the reaction rates and selectivity [53].  Figure 3 displays the XRD patterns of CaO and Al2O3 material prior to calcination and after the catalyst was synthesised. The results confirmed the characteristic peaks of 2θ ranging from 18° to 80°. Table 1 shows that there was an even distribution of lime and portlandite for CaO while in Figure 3b, Al2O3 support can be seen to have appeared at intensified peaks of 25.55°, 35.11°, 43.30°, 52.49°, 57.43° and 68.13°, These peaks reaffirmed the presence of rhombohedral Al2O3. Face-centered cubic CaO peak was found at 32.20°,   Figure 3 displays the XRD patterns of CaO and Al 2 O 3 material prior to calcination and after the catalyst was synthesised. The results confirmed the characteristic peaks of 2θ ranging from 18 • to 80 • . Table 1 shows that there was an even distribution of lime and portlandite for CaO while in Figure 3b, Al 2 O 3 support can be seen to have appeared at intensified peaks of 25 Figure 3a, these peaks correspond to the crystal planes of CaO and its cubic shape [54,55]. The CaO/Al 2 O 3 pattern also indicated small peaks of rhombohedral CaCO 3, hexagonal Ca (OH) 2   The specific surface area and pore volume were determined by the nitrogen adsorption-desorption technique summarised in Table 2, using Brunauer-Emmett-Teller (BET). The nitrogen isotherms recorded in Figure 4 for CaO/Al2O3 showed hysteresis over the relative pressure. The N2 isotherms exhibited a typical s-shaped behavior of type IV with a type H1 desorption hysteresis loop as categorised by IUPAC [56][57][58], indicating a potential presence of relatively wide cylindrical pores [59,60], which shows characteristics of The specific surface area and pore volume were determined by the nitrogen adsorptiondesorption technique summarised in Table 2, using Brunauer-Emmett-Teller (BET). The nitrogen isotherms recorded in Figure 4 for CaO/Al 2 O 3 showed hysteresis over the relative pressure. The N 2 isotherms exhibited a typical s-shaped behavior of type IV with a type H1 desorption hysteresis loop as categorised by IUPAC [56][57][58], indicating a potential presence of relatively wide cylindrical pores [59,60], which shows characteristics of a mesoporous material [61,62].
the study by Stankovic [64], the effect of calcination temperatures (425 °C, 450 °C, 475 °C, 500 °C) on the yield of biodiesel was evaluated with an inference that 475 °C gave the highest yield. After applying the same calcination temperature (475 °C), the pore diameter in this study increased to 24 nm, which is superior by showing better permeability with an increased surface area. As seen in Table 2, this assisted in the transesterification of sunflower waste to biodiesel with a maximum yield of 98% using a lower catalyst weight and ratio (solid base: solid acid) compared to that used in achieving similar yields by Elias et al. [65]. Additionally, the yield found was a lot more than that reported by Marinkovic et al. when a high catalyst amount of 5.5 wt% was used prepared at high calcination of 700 °C [66].

GC Analysis
The estimation of fatty acids content within each feedstock and the determination of fuel properties shown in Table 3 were determined by employing the GC. With double bonds being less stable than single bonds, their presence in the fatty acids affected the iodine number, viscosity, melting point, the efficiency of combustion and particulate matter formation related to soot [67], while improvement of average unsaturation helped with upgrading low-temperature performance but decreased the cetane number and caused poor oxidation stability [68]. Saturated fatty acids on other hand played a huge role in the cold flow properties relating to viscosity [69]. ASTM recommend viscosity of 1.9-6 mm 2 /s at 40 °C for biodiesel [70], and the high viscosity of vegetable oils prevents its direct usage The calculated specific area, pore volume and pore diameter for pure Al 2 O 3 and calcined 75% CaO supported on 25% Al 2 O 3 are presented in Table 2. Synthesised catalyst had a surface area of 13.0006 m 2 /g and Al 2 O 3 had 0.6239 m 2 /g, while pore volumes and diameters were 0.079732 cm 3 /g, 0.000857 cm 3 /g, 24.0371 nm and 5.9147 nm for prepared catalyst and alumina, respectively. An increase in surface area of CaO/Al 2 O 3 catalyst was observed after impregnating 75 wt% metal oxides onto alumina and thermal treatment. There was a significant increase in pore volume and pore size after the addition of CaO, which contributed to the liquid-solid heterogeneous phase reaction and offered enough of a reaction surface area for the transformation of waste oil into biodiesel.
Recent studies showed that CaO calcined at low temperature (500 • C) possesses a surface area of 5.2 m 2 /g and mean pore diameter of 11.9 nm [63], while the corresponding properties of the catalyst samples calcined at high temperatures (700-950 • C) changed but not to a substantial extent [61,63]. It seems that the textural characteristics of CaO used in the experiment (from CaO-500 • C to CaO-900 • C) are favorable for a liquidsolid heterogeneous phase reaction and provide a sufficient reaction surface area for the conversion of large triglyceride molecules. Significantly, the structural properties of CaO catalyst in the production of biodiesel effectively reduce greenhouse gas emissions. Nevertheless, in the study by Stankovic [64], the effect of calcination temperatures (425 • C, 450 • C, 475 • C, 500 • C) on the yield of biodiesel was evaluated with an inference that 475 • C gave the highest yield. After applying the same calcination temperature (475 • C), the pore diameter in this study increased to 24 nm, which is superior by showing better permeability with an increased surface area. As seen in Table 2, this assisted in the transesterification of sunflower waste to biodiesel with a maximum yield of 98% using a lower catalyst weight and ratio (solid base: solid acid) compared to that used in achieving similar yields by Elias et al. [65]. Additionally, the yield found was a lot more than that reported by Marinkovic et al. when a high catalyst amount of 5.5 wt% was used prepared at high calcination of 700 • C [66].

GC Analysis
The estimation of fatty acids content within each feedstock and the determination of fuel properties shown in Table 3 were determined by employing the GC. With double bonds being less stable than single bonds, their presence in the fatty acids affected the iodine number, viscosity, melting point, the efficiency of combustion and particulate matter formation related to soot [67], while improvement of average unsaturation helped with upgrading low-temperature performance but decreased the cetane number and caused poor oxidation stability [68]. Saturated fatty acids on other hand played a huge role in the cold flow properties relating to viscosity [69]. ASTM recommend viscosity of 1.9-6 mm 2 /s at 40 • C for biodiesel [70], and the high viscosity of vegetable oils prevents its direct usage in diesel engine [69] since this leads to the formation of deposits in the engine due to incomplete combustion [71]. As illustrated in Table 4, Waste palm oil (WPO) had a high viscosity of 47.5 cSt followed by 37.1 cSt for waste sunflower oil (WSO), which corresponds with their degree of saturated fatty acid, as seen in Table 3. The density of WSO and WPO in this study were found to be 0.9212 and 0.9168 g/cm 3 , respectively. The flashpoints reported in this study were above the minimum requirement supported by the findings by [72][73][74][75]. It was observed that fresh oils had lower acid, nitrates, sulphates and glycol as compared to their respective waste oils; this is due to degradation and contaminations resulting from over usage through cooking and contact with other chemicals. This creates FFA and accelerates the oxidation process.   Table 4 shows the properties of produced biodiesels of palm (PB100) and sunflower (SB100) from waste palm oil (WPO) and waste sunflower oil (WSO). According to the results of the biodiesels produced, most parameters met the specification set for use of biodiesel in diesel engines. These properties are crucial in fuel quality, performance, transportation and storage [76]. Notably, they depend on the feedstock used in the synthesis, which subsequently relates to the degree of saturation as seen in Table 3. Sunflower biodiesel is less flammable as indicated by a higher flashpoint of 175 • C, while palm biodiesel had 170 • C, which is preferred for handling and storage purposes [77]. This is because biodiesel and mineral diesel differ by 85% since the latter is usually above 150 • C [78]. In terms of the performance of palm, biodiesel was better since it had a high density, leading to a high mass of injected fuel causing more heat and creating more carbon, and therefore creating more power [79]. Additionally, oxidation stability in PB100 was superior, allowing for long-time stability at unfavourable conditions due to less polyunsaturated fatty acids in original feedstock [17], while for degradation during storage as indicated by acid number [72], sunflower biodiesel was the better fuel with a lower acid rate of 0.25 wt% which was below the standard limit and low compared to 0.55 wt% for palm biodiesel. Fuel atomisation was better in sunflower biodiesel, as indicated by reduced viscosity meeting standardisation [80]. Contaminants as indicated by the particulate matter of sulphates decreased in biodiesel from waste oils while nitrates increased as a result of more oxygen found in biodiesel [13,81]. Soot as well as glycol, which were higher in sunflower biodiesel, indicated more chances for incomplete combustion. Overall, sunflower biodiesel showed preferred fuel qualities; however, it also showed the possibility of lower oxidation stability under harsh conditions over longer storage time, as well as the possibility of incomplete combustion. Table 5 represents the content of major and some minor elements found in virgin sunflower (VSO) oil, virgin palm oil (VPO), waste sunflower oil (WSO) and waste palm oil (WPO), as well as produced biodiesels. P, S and Zn are present in feedstocks since they are taken from the soil and are a result of fertilisers used during cultivation [82], while Ca, K, Mg, Na and P are usually introduced through the production process [83], and can lead to undesirable combustion if present at high concentrations. A report by Sánchez et al. [37] found that Al, Fe, Mn and Zn are minor elements that relate to the soil characteristics, which explains their presence in the virgin oils. There was an increase in phosphorus from 17.625 mg/L and 31.937 mg/L for virgin sunflower and palm oils to 21.264 mg/L and 44.455 mg/L for waste sunflower and palm oils, respectively. The absence of Mg and K in both sunflower and palm virgin oils was observed, while less than 0.068 mg/L of Mg and 0.012 mg/L of K was seen in WPO, though cooking using salts increased the waste produced [37]. A report by Avila Orozco et al. [83] showed that Na, K, Ca, S and P came from raw material or chemical reagents. Lyra et al. [84] reported that their presence could have been incorporated due to the washing process with water. Therefore, since CaO/Al 2 O 3 was the catalyst used in synthesizing the biodiesels used in this study, a huge increase in Ca after production was seen from 0.025 mg/L and 0.345 mg/L to the drastic increment of 27.559 mg/L and 23.401 mg/L in biodiesel from waste sunflower and palm, which was associated with the sticking of injection or deposit on parts [85]. Sunflower methyl esters produced had lower elemental contaminates than palm methyl esters, which relate to better fuel quality but in terms of Ca, SB100 was higher, which would increase the rate of oxidation [35]. According to standard requirements set by ASTM D6751 and EN 14214, Ca+Mg should be a maximum of 5 mg/L [86]. SB100 and PB100 failed this test which is of great concern since high levels of Ca and Mg form deposits [87], which accelerate oxidation reaction [40]. Nevertheless, elements of Na, Fe, P and Al were reduced after the conversion of waste feedstocks to biodiesel meeting specifications set. Operational problems caused by high levels of Na and K through corrosion [88], the positioning of catalytical converters and the ability of the after-treatment system were eliminated due to deterioration caused by high P in fuel [89,90] and because sulphur is amongst the most concerning elements [40]. A high S content can affect the performance of engines [91], and the maximum limit set for sulphur in biodiesel is 10 mg/L [70,92]. It was observed that both biodiesels passed this test, which reduces corrosion in fuel containers [12]. The main source of metals in vegetable oil is either its presence in raw material or contact with the manufacturing process and storage [40], as degradation and contamination happen due to undesirable compounds in the engine [31]. The presence of inorganic constituents in biodiesel can affect the quality of the fuel and cause the malfunctioning of engines [87], and since different materials are used for storage containers and engine parts, there is an issue with compatibility [93]. Corrosion in biodiesel is mainly due to the component nature and composition of biodiesel, as well as the environment [12,94]. Metallic storage tanks such as stainless steel and Al are normally used for storage [95], while in automobiles, the fuel is in direct contact with various parts of the engine like the fuel pump, fuel injector, pistons and piston rings, which are made of Cu, Al, brass-Br (copper-rich alloy) and bronze [93]. Meanwhile, Cu has a huge effect on oxidizing biodiesel [96] and assessing Cu, Fe, and Zn is very crucial since along with Ni, Sn and brass, they can affect stability through oxidation [97]. Figures 5 and 6 illustrates the degradation of metal contents in biodiesel with different fatty acids composition by the Rancimat method of EN 14112 specification with samples held at a temperature of 110 • C. It is clear that all metal contaminants had an influence in promoting oxidation in palm and sunflower biodiesel with a large effect within palm biodiesel, as these metals initiate the formation of free radicals [98]. As the concentration of metals increased, the oxidation stability decreased; however, after the concentration of 2 ppm, the induction period was not constant, as was previously reported by [99]. The results indicate that Fe greatly decreased the oxidation stability more than Cu or Zn in both biodiesels. This was strongly pronounced from 300 ppm while Cu showed a significant influence at 100 ppm onward in palm biodiesel. In sunflower biodiesel meanwhile, a gradual reduction was observed through to 700 ppm. Contrarily, the literature reported Cu to reduce oxidation stability more than Fe or Zn [91,100,101] and the induction period became constant after 2 ppm [99,102]. Contrarily, this study had Fe as the most catalytic effect in reducing the induction period and it became constant after 500 ppm of metal concentration for both biodiesels. Additionally, Palm biodiesel proved to have to degrade more and was found to have the most corrosiveness [12].

ICP-OES Analysis in Virgin, Waste Sunflower and Palm Oil and Their Biodiesels
> carbon steel > Al > stainless steel, while in the study by Fazal et al. [39], it was discovered that palm biodiesel degraded in the order of Cu > brass (Br) > Al > cast iron (CFe). Furthermore, in the experiment by Nurul et al. [107], where they investigated the corrosive behaviour of different steel materials which are mainly iron found in stainless steel, corrosion was localised while mild and galvanised steels were generalised.   > carbon steel > Al > stainless steel, while in the study by Fazal et al. [39], it was discovered that palm biodiesel degraded in the order of Cu > brass (Br) > Al > cast iron (CFe). Furthermore, in the experiment by Nurul et al. [107], where they investigated the corrosive behaviour of different steel materials which are mainly iron found in stainless steel, corrosion was localised while mild and galvanised steels were generalised.   Sunflower biodiesel showed the highest corrosiveness impact of metals with Iron (Fe) followed by Zn and Cu; however, at a concentration of 700 ppm, Cu was the most degraded metal. For PB100, the addition of metal concentrations lower than 100 ppm resulted in Cu having more corrosiveness followed by Zn and Fe but after 300 ppm, Fe was more corrosive than Cu and Zn. This was supported by the studies of Baena and Calderón and Sentanuhady et al. [103,104], who found the metal that was most prone to corrosion in biodiesel is Cu. Also, Shiotani and Goto [100] reported in their study that in PB100, Cu was found to have more degradation of oxidation followed by tin, iron, zinc and aluminium. Additionally, Thangavelu et al. [105] reported that copper had a higher corrosion rate than aluminium and stainless steel in that order. The investigation by Hu et al. [106] also reported that corrosion in biodiesel from rapeseed oil was in the order of stainless Cu > carbon steel > Al > stainless steel, while in the study by Fazal et al. [39], it was discovered that palm biodiesel degraded in the order of Cu > brass (Br) > Al > cast iron (CFe). Furthermore, in the experiment by Nurul et al. [107], where they investigated the corrosive behaviour of different steel materials which are mainly iron found in stainless steel, corrosion was localised while mild and galvanised steels were generalised.

Preparation of Bifunctional Catalyst (CaO/Al 2 O 3 )
The bifunctional (CaO/Al 2 O 3 ) catalyst was synthesised by preparing an aqueous solution made of 37.5 g primary reagent grade of calcium oxide and 12.5 Aluminium oxide support. The wet impregnation method was utilised [108]. However, a minor modification was done by using precursor salt of commercial CaO, which was dissolved in distilled water. Thereafter, the introduction of alumina onto the precursor was carried out in a 100 mL flask. The mixture was vigorously stirred at room temperature for 4 h using an overhead stirrer (SCIENTECH Inc., Boulder, CO, USA) set at 600 rpm, as reported in the study by Zabeti et al. [109]. The mixture was filtered under vacuum with grade 1 Whatman filter paper (Merch, Darmstadt, Germany). Thereafter, drying was accomplished in a static oven (Scientific, Kyalami, South Africa) set to 120 • C for 18 h. Prior to activation, the dried paste was crushed into fine powders by the use of pestle and mortar. To calcine the catalyst, a muffle furnace which was set at 475 • C, was used for 5 h. with a ramping rate of 5 • C/min [64,108]. After calcination, the catalyst was left to cool down at room temperature and was then transferred to a closed glass vial for storage.

Transesterification
In this study, the 75%CaO/25%Al 2 O 3 catalyst was used to investigate the effect of conversion rate per catalyst (rate of yield) through a transesterification reaction and its contribution towards the elemental content within biodiesel. The reaction was carried out in a 250 mL round glass flask connected to a condenser, which avoided evaporation by having inlet and outlet systems to cool down the temperature. Waste cooking oil was added into the round glass flask with a thermometer placed inside it. The oil was pre-heated to 40 • C and the flask was slowly introduced into a water bath on a hotplate. A total of 100 g of methanol to oil ratio was mixed with 2.5 wt% of catalyst synthesised and poured into a 250 mL round-flask which had a stirrer; the mixture was then stirred vigorously. The hotplate was roughly set at 110 • C and as the temperature reading on the thermometer increased to 60 • C, the reaction was kick-started. The inlet and outlet flow of water that was connected to the condenser assisted in maintaining a constant temperature throughout the reaction and the mixing speed was set at 1300 rpm. After the reaction was completed, the products were poured into centrifuge tubes with equal masses and were centrifuged at 2200 rpm using Ohaus Multi Centrifuge for 10 min. Thereafter, samples were poured into separatory funnels for the separation of biodiesel and glycerol into phases, while solids were left in the centrifuge tubes. Distilled water used in the biodiesel washing was heated to a temperature of 50 • C. During the washing stage, three times the amount of water to biodiesel was used. This allowed for clean biodiesel, as the washed water was clear. The biodiesel was thereafter placed on a hotplate in a beaker and a small amount of Na 2 SO 4 was used to dry any trace amount of water that might have been left in the biodiesel. The product was then left to cool and stored for analysis.

Characterisation Techniques
The Infrared spectral was performed using a spectrum high performance TWO LITA FTIR instrument (PerkinElmer, Inc., Walthan, MA, USA) equipped with a lithium tantalate detector (LiTaO 3 ) and Spectrum 10™ software. All spectra were collected at a range of 400 to 4000 cm −1 with a resolution of 4 cm −1 using an average of 10 scans.
The morphology of the catalyst was assessed using a Field-Emission Scanning Electron Microscope (The Nova NanoSEM 230, Hillsboro, OR, USA) equipped with an in-lens secondary electron and backscattered electron detectors. The element was operated at an accelerating voltage of 5 kV using TESCAN MIRA.
The crystalline phases present were identified using a multipurpose X-ray diffractometer (XRD), D8-Advance (BRUKER AXS, Karlsruhe, Germany), which was operating in a continuous scan in locked coupled-mode using Cu-Kα radiation with a wavelength (λ) of 1.5406 Å at 40 kV and 40 mA. The measurements were run within a range in 2θ (0.5 • to 80 • ) with a typical step size of 0.034 • . A position-sensitive detector, Lyn-Eye, was used to record diffraction data at a screening speed of 0.5 s/step, which is equivalent to an effective time of 92 s/step for a scintillation counter. The XRD phases were identified using an Internal Center for Diffraction Data (ICDD) PDF database 1999 using EVA software from BRUKER.
The Brunauer-Emmett-Teller (BET) was employed to determine the surface area, pore volume and pore size distribution of the synthesised catalysts using TriStar II 3020 Analyser version 2.00 (Micromeritics, Instruments Corporation, GA, USA) at a liquid nitrogen and operation bath temperature of 77.350 K. The BJH method was used for calculating pore volume distribution and average pore diameter while for the surface area, BET analysis was used. The sample was degassed overnight at 200 • C, while the reference Al 2 O 3 was degassed at 300 • C for 3 h to obtain reasonable adsorption-desorption isotherms.
The fatty acids concentration was obtained using GC 7890A (Agilent Technologies, Inc, Waldbronn, Germany) detailing components within feedstocks, as materials were separated from each other by the number of their constituent atoms. This follows ASTM 6584 and EN 14214 standardisation.
Physico-chemical properties of feedstock and biodiesel were analysed for properties such as acid number, density, viscosity, oxidation stability, flash point and total contamination using conventional methods according to ASTM and EN methods.

Conclusions
A highly active bifunctional catalyst of CaO/Al 2 O 3 was prepared by the wet impregnation method and used for its transesterification reaction. The catalyst was found to be suitable for the conversion of oils with a high FFA such as waste cooking oils (>15% FFA) to FAME; however, it influenced the increase of concentration of Ca within biodiesel. Biodiesel properties were evaluated according to ASTM and EN methods. The quality was highly influenced by the molecular structure, the chain length and the degree of saturation in the feedstock used for biodiesel production. From the results obtained, it was determined that biodiesels produced from waste palm oil had longer oxidation stability than those produced from waste sunflower oil. Additionally, with the evaluation of the oxidation stability through the addition of Fe, Cu and Zn metal powders to biodiesels concentrations of 2-700 ppm, the findings showed that all metals had an impact on reducing the induction time for concentrations of 2-700 ppm. The intensification in oxidation stability was influenced by the increase in metal concentrations and the type of biodiesel produced. In both biodiesels, Fe decreased oxidation stability and significantly failed EN specifications in PB100 from 500-700 ppm and in all concentrations of SB100. Furthermore, a remarkable decrease of Cu in SB100 at a concentration of 700 ppm was also observed and the order of overall corrosiveness of metals in sunflower biodiesel was Fe > Zn > Cu and the equivalent in palm biodiesel was Fe > Cu > Zn, with most metals impacting on induction time reductions.