Transesterification Of Oil Research Articles

Production of biodiesel by using CaO nano-catalyst synthesis from mango leaves extraction

Development and population expansion have the lion's share of driving up the fuel cost. Biodiesel has considerable attention as a renewable, ecologically friendly and alternative fuel source. In this study, CaO nanocatalyst is produced from mango leaves as a catalysis for the transesterification of waste cooking oil (WCO) to biodiesel. The mango tree is a perennial plant, and its fruit holds significant economic worth due to its abundance of vitamins and minerals. This plant has a wide geographical range and its leaves can be utilized without any negative impact on its growth and yield. An analysis was conducted to determine the calcium content in the fallen leaves, revealing a significant quantity of calcium that holds potential for utilization. The catalyst was characterized by different analytic techniques such as XRD, SEM-EDS, FT-IR, and BET analyses. Several parameters impacted on the transesterification process were exploited by conventional transesterification (batch). The result revealed that the optimum reaction was reached at a methanol to oil ratio of 50% w/w, catalyst loading of 3%, temperature of 65℃ and reaction time of 1.5 h with a yield of 93.21%, and the activation energy of the transesterification reaction was found to be 38.906 KJ mol-1. The reaction was verified to be irreversible pseudo-first order based on a linear Arrhenius plot and a high R2 value. The catalyst shows good stability and catalytic activity when it is reused and the yield was found to be 80.293% in the 5th cycle.

Novel Preparation and Characterization of Zinc Ricinoleate Through Alkali Catalysis

The enhanced thermal and chemical stability of Zinc oxide-based materials make them excellent candidates for the removal of odor-producing pollutants and compounds. The zinc salt of ricinoleic acid, commonly known as zinc ricinoleate, is viewed as the top performer. This article describes an innovative two-step synthesis of zinc ricinoleate, where the first step consists of the preparation of an intermediate compound, methyl ricinoleate, which is synthesized via transesterification of castor oil with methanol and catalyzed by sodium hydroxide. The second step comprises the preparation of zinc ricinoleate through the saponification of methyl ricinoleate in the presence of zinc oxide particles. XRD, FTIR, and NMR spectroscopies confirmed the synthesis of methyl ricinoleate and zinc ricinoleate. HR-SEM and AFM images showed the formation of larger particles, while the thermal stability of the materials was confirmed by TGA.

Utilization of waste from paper industry as a heterogeneous base catalyst for the synthesis of biodiesel

AbstractTo meet the pressing demand for alternative biofuel in the contemporary world, the production cost of biodiesel has to be decreased. Hence, this work addresses the usage of CaCO3‐rich industrial waste produced in a local paper industry in Assam, India for the synthesis of a heterogeneous catalyst for biodiesel synthesis. The collected lime sludge waste was subjected to calcination at 800°C for 3 h producing a CaO‐rich catalyst which was then employed in the transesterification of cottonseed oil. The optimized reaction conditions obtained were 5 wt% catalyst concentration, oil to methanol molar ratio of 1:12 at 65°C temperature, and 3 h of reaction time. The catalyst's reusability was evaluated up to four cycles. Besides, the prepared catalyst has been characterized using Fourier transfer infrared spectroscopy (FTIR), powder X‐ray Diffraction (p‐XRD), Scanning Electron Microscope (SEM), Energy Dispersive X‐ray analysis (EDX), and Brunauer–Emmett–Teller (BET) techniques and its basicity was measured using Hammett indicators. Moreover, the biodiesel obtained was characterized with 1H‐nuclear magnetic resonance (NMR), 13C‐NMR, Gas Chromatography‐ Mass Spectrometry (GC–MS), and FTIR techniques. A biodiesel yield of 98.03% was achieved and the quality of biodiesel formed during the transesterification of CSO also conforms to EN 14214 and ASTM D 6751 standards. Thus, our study highlights the sustainability and the potential for future industrial application of paper industrial waste in the production of biodiesel.

Bioinspired Synthesis of Novel Different Nanoparticles and its Utility in Biodiesel and Animals Applications

Because of its ability to speed up the reaction, the catalyst is critical to its success. Most catalysts are either homogeneous or heterogeneous. It has been shown that utilizing a heterogeneous catalyst, which is easier to remove from the product after the reaction has been finished. Because of the large surface area of the Nano-catalyst results in high catalytic efficiency. To enhance the performance of catalysts a range of various types of support materials have been used. SO42--ZnO and So42-/TiO active acid catalyst was prepared and characterized. ZnO nanoparticles catalyst synthesized by precipitation of zinc nitrate for comparison with supported catalyst. Sulphated zinc oxide (SO42--ZnO) and sulphated titania (SO42-/TiO) catalysts were synthesized using impregnation methods, to test their efficacy in biodiesel production. Various waste oils from different wastes such as mutton or beef tallow, chicken fat, and methanol are preferred to use during the esterification of waste animal fat oils using solid acid catalysts to produce biodiesel. Biodiesel synthesis generates a substantial amount of glycerol as a byproduct. Effect of optimum parameters such as temperature 60 degree centigrade (°C) shown 90% yield, time 1 hour resulted in 85% yield, catalyst dose 2wt% resulted in 80% yield, stirring speed 250rpm resulted in 80% yield, methanol to oil ratio12:1 resulted as 85.5% yield for transesterification of waste fat oil. It is valuable that the supported acid catalysts showed more yield than simply synthesized ZnO nanocatalyst similarly sulphated zinc oxide showed more FAME yield than sulphated titania.

Optimization of Dissolved Air Flotation (DAF) process for the treatment of oily water from biodiesel production

Biodiesel production has become one of the most efficient ways of diversifying the energy matrix. However, the increase in biodiesel production increases the generation of wastewater. Therefore, this study aimed to characterize the wastewater generated in the biodiesel washing process, obtained by the alkaline transesterification of sunflower oil, and to evaluate its treatment by the dissolved air flotation (DAF) system, using a Central Composite Rotational Design (CCRD). The first DCCR was carried out with 4 independent variables: pH, Coagulant Dose (CD), Polymer Dose (PD), and Recirculation Rate (RR), with the response variables being apparent color removal and turbidity removal. Based on the results of the first DCCR, optimization tests were designed with DC and DP as independent variables and apparent color, turbidity, COD, and oil and grease (OG) as response variables. The process showed high apparent color and turbidity removal efficiency. The best results were obtained in tests 10 (DC = 1545 mg.L-1 and DP = 1050 mg.L-1) and 3 (DC = 700 mg.L-1 and DP = 8.8 mg.L-1), with the removal of 99.88% and 99.22%, respectively. For the COD and OG parameters, the best results were observed in tests 8 (DC= 555 mg.L-1 and DP= 6 mg.L-1) and 5 (DC= 1050 mg.L-1 and DP= 6 mg.L-1), with 98% and 99.42% removal, respectively. FAD treatment using the combination of coagulant and cationic polymer proved to be highly efficient in treating wastewater from biodiesel production.

Transesterification of waste cooking oil for biodiesel production using alkaline-modified graphitic carbon nitride heterogeneous catalyst

ABSTRACT Developing efficient, stable, cost-effective, and environmentally benign heterogeneous catalysts for transesterification is highly required for sustainable biodiesel production. The present study explores the biodiesel production from waste cooking oil (WCO) using graphitic carbon nitride (g-C3N4) and its alkaline-modified nanocatalyst. The catalysts were characterised by X-ray diffraction (XRD), Scanning electron microscopy (SEM), Energy Dispersive X-ray spectroscopy (EDS), and Fourier transform infrared spectroscopy (FTIR). From the XRD analysis, crystalline sizes of g-C3N4 and alkaline g-C3N4 were found to be 26 and 29 nm, respectively. Transesterification of WCO was carried out at 60 °C for a reaction time of 2 h using 2 wt.% of g-C3N4 and alkaline g-C3N4. Transesterification reaction catalysed by alkaline-modified g-C3N4 was found with a higher yield of biodiesel (89%) than the biodiesel yield (78%) with transesterification reaction catalysed by g-C3N4. The recyclability of both catalysts was also evaluated by reusing them for up to the 5th cycle. The obtained biodiesel was analyzed by using FTIR and GC-MS. The synthesised biodiesel was found to have significant level of monounsaturated fatty acids and saturated fatty acids, which make it usefuel for use as fuel. Some physicochemical properties of the obtained biodiesel were also calculated and found appropriate as per the American Society for Testing and Materials (ASTM) standards. With high reusability and good catalytic activity, the synthesised alkaline-modified g-C3N4 can be employed as a viable option for biodiesel production from WCO.

Green and economical transesterification of castor oil for biodiesel production via a novel bentonite based Li2SiO3-LiAlO2 composite: Process technology & production feasibility

In our work, a highly efficient Li2SiO3-LiAlO2 composite was designed via a simple solid-state reaction using bentonite as raw material and successfully applied to the transesterification of castor oil with methanol for biodiesel production. The preparation processes for the bentonite-based Li2SiO3-LiAlO2 composite (Li/Bent) were optimized, and the prepared Li/Bent catalyst was characterized using a variety of experimental techniques. The maximum oil conversion to biodiesel of 97.16% was obtained under reaction temperature of 65 °C, reaction time of 90min, catalyst amount of 4wt.%, and methanol/oil molar ratio of 15:1. The possible mechanisms of the reaction process were revealed. The preliminary analysis of technical feasibility for the production showed that Li/Bent composites catalyzed castor oil production of biodiesel had competitive advantages in terms of market demand, industrial policy, process technology, environmental impact and economic benefits. The high efficiency and good stability of the catalyst reflect the technical advantages of the process. According to the study of environmental factor and process mass index, the synthesis process of biodiesel generated low waste, which was a green and environment-friendly process. Finally, the economic evaluation showed that the biodiesel production from castor oil catalyzed by Li/Bent catalyst was a cost-effective and low risk process.

The prediction of biodiesel production yield from transesterification of vegetable oils with Machine learning

Biodiesel is a renewable energy produced from transesterification of vegetable oils in the presence of various catalysts. The biodiesel production yield depends on types of feedstocks, reaction time, temperature, ratio of methanol to oil, and types of catalysts. Machine learning can be applied for prediction of biodiesel yield in a single process but the combination of biodiesel production processes, including a variety of alkali and acid catalysts, should be investigated. This work developed the modeling by using machine learning to predict the biodiesel yield of alkali catalysts and acid catalysts. The machine learning algorithms consisted of artificial neural network (ANN) and artificial neural network – particle swarm optimization (ANN-PSO). The proposed model was examined for Case I (alkali process) and Case II (combination process). For Case I with 19 input variables and a single output variable, the ANN with the trainlm algorithm and the Tansig- Tansig activation function was the most suitable model, offering the MAPE of 1.3510 and R square of 0.99272. While in Case II, the ANN with the trainbr algorithm performed the most accurately in terms of R square of 0.97229 and MAPE of 2.32145. Finally, the feature importance for Case I and Case II presented that the molar ratio of methanol to oil was the most important variable for the prediction of biodiesel yield.

Evaluation of Microbial Phospholipase and Lipase Activity Through the Chromatographic Analysis of Crude, Degummed, and Transesterified Soybean Oil for Biodiesel Production.

The present study aimed at synthesizing fatty acid methyl esters in a combined enzymatic method by applying degumming and transesterification of soybean oil. A soluble lipase from Serratia sp. W3 and a recombinant phosphatidylcholine-preferring phospholipase C (PC-PLC) from Bacillus thuringiensis were used in a consecutive manner for phosphorus removal and conversion into methyl esters. By applying 1% of recombinant PC-PLC almost 83% of phosphorus was removed (final content of 21.01mg/kg). Moreover, a sensitive and selective high-performance liquid chromatography method coupled to tandem mass spectrometry was applied to obtain a comprehensive lipid profile for the simultaneous evaluation of phospholipids removal and diacylglycerol (DAG) increase. A significant increase for all the monitored DAG species, up to 138.42%, was observed by using the enzymatic degumming, in comparison to the crude sample, resulting in an increased oil yield. Serratia sp. W3 lipase was identified as a suitable biocatalyst for biodiesel production, converting efficiently the acylglycerols. The results regarding the physical-chemical characteristics show that the cetane level, density and pour point of the obtained biodiesel are close to current regulation requirements. These findings highlight the potential of a two-step process implementation, based on the combination of lipase and phospholipase, as a suitable alternative for biodiesel production.

Optimizing Algal Oil Extraction and Transesterification Parameters through RSM, PCA, and MRA for Sustainable Biodiesel Production

This study presents a comprehensive optimization of algal oil extraction and transesterification for sustainable biodiesel production. Freshwater Spirogyra algae underwent Soxhlet extraction using n-hexane. response surface methodology (RSM), principal component analysis (PCA), and multivariate regression analysis (MRA) were employed to investigate the effects of biomass–solvent ratio (BSR), algae particle size (APS), and extraction-contact time (E-CT) on algal oil yield (AOY). The extracted oil was then converted to biodiesel via transesterification, and the impacts of the methanol–oil ratio (MOR) and transesterification-contact time (T-CT) on biodiesel conversion efficiency (BCE) were analyzed. Results demonstrate that optimal BSR, APS, and E-CT for maximal AOY are 1:7, 400 µm, and 3–4 h, respectively. For transesterification, a MOR of 12:1 and a T-CT of 4 h yielded the highest BCE. Predictive models exhibited exceptional accuracy, with R2 values of 0.916 and 0.950 for AOY and BCE, respectively. The produced biodiesel complied with ASTM D6751 and EN 14214, showcasing its potential for renewable energy applications.

Experimental and computational investigations of biodiesel production from castor oil using Li-doped salmon fish bone-supported lanthanum oxide catalyst in a micro-reactor

Ensuring efficient and sustainable biodiesel production is essential for addressing environmental concerns and meeting global energy demands. This study aims to optimize the transesterification of castor oil through the development of a distinctive Li-doped-salmon fish bone (SFB)-supported La2O3 composite catalyst within a micro-reactor setup. The optimal catalyst (3 % Li/SFB-La) was thoroughly evaluated for its physicochemical features employing a range of characterization techniques, including XRD, XPS, BET, FESEM, TEM, TGA/DSC, and FT-IR. According to density functional theory (DFT) calculations, the function of Li dopants, which have a lower electronegativity (0.98) compared to La (1.1), is to enhance the charge transfer capability of La sites, thereby increasing their reactivity with triglycerides. In the interim, we determined the optimized reaction conditions: a 6:1 methanol/oil molar ratio and a 5 wt % catalyst loading at 338 K. Under these parameters, an impressive 99.38 % conversion was achieved within 1.5 h. Furthermore, the 3 % Li/SFB-La composite catalyst exhibited remarkable stability, retaining its high activity throughout 7 cycles without any significant loss of efficacy. Moreover, the transesterification reaction kinetics were thoroughly investigated, revealing a reaction rate constant of 1.17 h−1 and an activation energy of 14.46 kJ/mol.

Production and optimization of biofuels from locally isolated algal biomass: Strategies for circular economy integration

In the present study, we investigated the potential of locally isolated algal strains as alternative energy sources for sustainable biofuel production. The focus of this study was to identify algal strains that are capable of accumulating oils rich in essential fatty acids. Algal samples were collected from different areas and 14 isolates were obtained. Among the various pretreatment methods tested, hydrothermal pretreatment using sulfuric acid at 95 °C yielded the best results, with sample IIB-14 containing more than 2% reducing sugars. These sugars were then used for fermentation with the S. cerevisiae strain, resulting in an ethanol concentration of 3.52% ± 0.2%. This holistic approach contributes to the development of low-cost and environmentally friendly alternatives to traditional energy sources. While algal biofuels offer a promising substitute for fossil fuels, further advancements are needed before they can be widely adopted in the fuel market. Among these, isolates IIB-8 and IIB-9 showed the highest oil yields of 22.84% and 24.69% (w/w), respectively. The specific environmental settings for optimal growth of these strains were determined, and the physicochemical parameters of the oils, including iodine value, viscosity, density, acid value, saponification value, unsaponifiable mass, and peroxide value, were analyzed. The transesterification of oils into fatty acid methyl esters (FAMEs) revealed the presence of significant amounts of fatty acids, including EPA, DHA, and linoleic acid. Moreover, the study also explored the potential of algal biomass for bioethanol production, addressing the sustainability concerns of renewable energy supplies. Hydrothermal pretreatment using sulfuric acid at 95 °C yielded the highest concentration of reducing sugars (>2%) in IIB-14. Sugar extracted from algal biomass was used for fermentation. The Saccharomyces cerevisiae strain used for the fermentation process yielded an ethanol concentration of 3.52% ± 0.2%. This holistic approach contributes to the development of low-cost and environment-friendly alternatives to renewable energy sources. Algal biofuels may offer a practical substitute for fossil fuels, but there is still a long way to go before they can enter the fuel market and are widely used.

Comparative analysis of Brassica carinata and fungal industrial lipases used for biodiesel production

Aim. To identify the genes of endogenous TAG-lipases in the genome of Abyssinian mustard, or carinata (Brassica carinata), and to analyze the similarity of their amino acid sequences with the industrial lipases of fungal origin. Methods. Genome-wide search for B. carinata TAG-lipase sequences was conducted out, annotation of the identified genes, alignment of their sequences, phylogenetic analysis was performed, as well as identification of conserved sequence motifs and functional domains of these proteins was done. Results. 13 TAG-lipase genes were identified in the genome of Abyssinian mustard, and their phylogenetic relations with camelina and fungal lipases was reconstructed. The domain structure of carinata TAG-lipases was analyzed, and the level of sequence divergence of their functional regions was also revealed. Conclusions. Fungal lipases were identified, which are most similar in terms of domain organization to the identified TAG-lipases of B. carinata, and therefore could potentially be used to increase the efficiency of transesterification of carinata oil.

Modeling the Effects of Temperature in Enzymatic Biodiesel Synthesis of Jatropha Oil: An Optimal Control Approach.

Biodiesel, an alternative to diesel, is produced through the enzymatic transesterification of vegetable oil or animal fats. Enzymatic transesterification of oil is gaining more importance, as this method possesses no such disadvantages that are associated with the chemical process. Temperature is the most important factor in enzymatic transesterification for biodiesel synthesis. In this study, a mathematical model is developed to understand the effects of temperature on the enzymatic transesterification of Jatropha curcas oil. Reaction rates are expressed as a function of temperature using an appropriate function, and the effects of temperature on the overall enzymatic system are investigated using the mathematical model. A suitable temperature is determined using the mathematical model, keeping the other reaction conditions unchanged that gives maximum yield. Furthermore, an optimal control problem (OCP) is formulated to identify the temperature control strategy that maximizes the biodiesel yield while minimizing production costs. Simulated outcomes obtained from the mathematical model are analogized with the experimental results to make them acceptable. The optimal profile of temperature is determined from the developed OCP, which maximizes the biodiesel yield.

Luffa oil transesterification prediction via adaptive neuro-fuzzy inference system using an acid-activated waste marble catalyst

Luffa oil transesterification prediction via adaptive neuro-fuzzy inference system using an acid-activated waste marble catalyst

Catalytic evaluation of eggshell‐based calcium methoxide over Al2O3 for biodiesel generation from waste cooking oil

AbstractShell‐derived materials are promising heterogeneous catalysts for biodiesel production due to their nontoxic and renewable nature, but they have the disadvantage of being highly leachable. To overcome this issue, Ca(OCH3)2 formed through the reaction of CaO with methanol, and supported in turn on Al2O3 is proposed as a catalytic system for the transesterification of fresh soybean oil and waste cooking oil (WCO). First, catalysts with several Al/Ca molar ratios (0.2, 0.5, and 0.8‐AC), as well as their precursors (CaO and Al2O3) alone, were tested at 60 °C, catalyst loading 6% wt, methanol‐to‐oil molar ratio (MOR) 10, for 1 h for fresh oil, and 3 h for WCO. The 0.2‐AC catalyst generated the highest biodiesel yield for both oils. The optimum operating conditions for WCO transesterification, determined by using a univariable approach, were 60 °C, 9 wt% catalyst loading, MOR of 12.5, and a reaction time of 3 h. These improved conditions led to yields higher than 90% for pure CaO and the 0.2, 0.5, and 0.8‐AC catalysts. The density, kinematic viscosity, and refractive index of the biodiesel obtained were measured.

Investigation into the Fuel Characteristics of Biodiesel Synthesized through the Transesterification of Palm Oil Using a TiO2/CH3ONa Nanocatalyst

Biodiesel is a renewable and sustainable alternative fuel to petrol-derived diesel. Decreasing the operating costs by improving the catalyst’s characteristics is an effective way to increase the competitiveness of biodiesel in the fuel market. An aqueous solution of sodium methoxide (CH3ONa), which is a traditional alkaline catalyst, was immersed in nanometer-sized particles of titanium dioxide (TiO2) powder to prepare the strong alkaline catalyst TiO2/CH3ONa. The immersion method was used to enhance the transesterification reaction. The mixture of TiO2 and CH3ONa was calcined in a high-temperature furnace in a range between 150 and 450 °C continuously for 4 h. The heterogeneous alkaline catalyst TiO2/CH3ONa was then used to catalyze the strong alkaline transesterification reaction of palm oil with methanol. The highest content of fatty acid methyl esters (FAMEs), which amounted to 95.9%, was produced when the molar ratio of methanol to palm oil was equal to 6, and 3 wt.% TiO2/CH3ONa was used, based on the weight of the palm oil. The FAMEs produced from the above conditions were also found to have the lowest kinematic viscosity of 4.17 mm2/s, an acid value of 0.32 mg KOH/g oil, and a water content of 0.031 wt.%, as well as the highest heating value of 40.02 MJ/kg and cetane index of 50.05. The lower catalyst amount of 1 wt.%, in contrast, resulted in the lowest cetane index of 49.31. The highest distillation temperature of 355 °C was found when 3 wt.% of the catalyst was added to the reactant mixture with a methanol/palm oil molar ratio of 6. The prepared catalyst is considered effective for improving the fuel characteristics of biodiesel.

Green hetero-alkali catalyst in optimized waste lard oil transesterification for biodiesel synthesis

Climate change in addition to the imminent depletion of the fossil fuel reserve has necessitated the search for a sustainable alternative fuel. In this research, the catalytic capability of a green heterogeneous alkali catalyst, thermally activated banana-plantain-peel-ash catalyst was examined in optimized waste lard oil (WLO) transesterification process in lard-oil-methyl-ester (LOME) synthesis. The catalyst was derived from a banana-plantain-peel-ash mixture and subjected to a calcination process while the catalyst properties were described via Scanning electron microscope-Energy dispersive atomic-x-ray-spectroscopy (SEM-EDX), X-ray diffraction-(XRD), Fourier Transform Infra-Red (FTIR) as well as Brunauer-Emmett-Teller (BET). Optimization of the waste lard oil transesterification process was conducted with the Desirability Explore Algorithm (DEA) in Central Composite Design (CCD) of Response Surface Methodology (RSM). A 99.9 % conversion of WLO to LOME was attained at the optimum reaction settings of 57 °C temperature, catalyst amount-2.5 wt%, time-1.5 h, and methanol to WLO molar ratio of 10.5:1 with a total desirability of 0.99 which was evaluated experimentally as 99 %. In the LOME synthesis procedure, the resulting empirical model demonstrated statistical significance and suitability based on its high F-value of 35.59 and infinitesimal p-value of less than 0.0001. The determined LOME fuel qualities met the applicable standard specifications (ASTM-D6751 and EN-14241) hence, have the potential to function as a diesel fuel substitute. The fused influence of WLO and the thermally activated bio-mixture catalyst was highly effective in biodiesel synthesis. Thus; a promising cheap feedstock source for green and sustainable biodiesel production was achieved.

Biodiesel Production from Edible Oil Using Heteropoly Acid Catalysts at Room Temperature

Edible oils are one of the renewable sources that enable the possibility of producing biodiesel sustainably. The transesterification of canola oil with methanol using cesium-modified phosphotungstic acid (Cs2.5H0.5PW12O40) as a heterogeneous catalyst was studied. Reaction conditions, specifically reaction time, catalyst loading, and the ratio of methanol to canola oil, were systematically explored. The canola oil conversion reached 55% at room temperature after 24 h. The reusability tests showed that the conversion of canola oil to biodiesel was maintained.

Kinetics and soft computing evaluation of Linseed oil transesterification via CD-BaCl-IL catalyst

A novel clay-doped ionic liquid and BaCl (CD-BaCl-IL) heterogeneous catalyst for biodiesel synthesis from linseed oil (LSO) was generated after 4 h of calcination at 600°C using Scanning Electron Micrograph (SEM), X-ray Diffraction (XRD), Brunauer-Emmett-Teller (BET), Fourier Transform Infrared Spectroscopy (FT-IR) and X-ray fluorescence (XRF) was used to evaluate the catalyst's processability. After optimization using response surface methodology (RSM), the second-order polynomial model was shown in the Analysis of variance (ANOVA) with R2 values of 0.9947, Adj R2 (0.9850), and Pred R2 (0.8594), demonstrating model acceptability. The maximum biodiesel yield (97.097 %) was obtained with 2.6 wt% catalyst, 6 mol/mol methanol/molar ratio, 1.5 h, 50 °C, and 400 rpm agitation. ANFIS predicted biodiesel yield more accurately than ANN (R2 = 0.999, MSE = 0.27594), with the lowest MSE (R2 = 0.99, MSE = 0.00038). Under optimal conditions, this study employed a kinetic model based on two elementary chemical processes: Eley-Rideal (ER) and Langmuir-Hinshelwood-Hougen-Watson (LHHW). The LHHW model accurately described CD-BaCl-IL catalyst experimental data at 50 °C, with favourable parameters, an R2 value of 0.9348, and a variance of 2.61E-8. The surface reaction between adsorbed triglyceride and alcohol dictated the rate-determining step. Temperature increased the rate, indicating an endothermic process. The reaction's activation energy and frequency factor were 10.22 kJ/mol and 6.41 h-1, respectively. Linseed biodiesel met the D6751 criterion.