Catalyst For Biodiesel Production Research Articles

Transesterification reaction time impacts on oxidation stability and acid number of biodiesel production from waste cooking oil

The scarcity of fossil fuels, environmental concerns, and the sharp rise in fossil fuel prices have driven scientists to search for alternative fuels. The characteristics of biodiesel have made the quest for high-quality biodiesel production particularly appealing. The use of waste cooking oil is a key component in reducing biodiesel production costs by 60-90%. Researchers have employed various types of transesterification reactions with both homogeneous and heterogeneous catalysts for biodiesel production; in this study, a 0.5% NaOH catalyst is used. The objectives of this study are to produce biodiesel fuel based on waste cooking oil, evaluate the impact of reaction time variation on the oxidation value and acid value of biodiesel produced from waste cooking oil, and statistically test the effects of reaction time on the oxidation value and acid value of biodiesel produced from waste cooking oil using analysis of variance (ANOVA). The optimum yield was obtained at a reaction time of 90 minutes, achieving 97%. The results for acid number and oxidation value for various reaction times complied with ASTM, EN, and SNI standards. Linear regression analysis of ANOVA for the acid number concluded that the P-value t3 is 0.399, which is greater than Alpha = 0.05, indicating that the variation in reaction time does not have a significant effect on the acid number. Linear regression analysis of ANOVA for the oxidation number concluded that the P-value t3 is less than Alpha (0.047 < 0.05), indicating that reaction time has a significant effect on the oxidation number.

Enhancing Sustainable Production of Biodiesel from Xanthoceras sorbifolia Bunge Oil Using Bio-Based Heterogeneous Catalyst

The swift exhaustion of natural oil reserves and worsening environmental issues have prompted the quest for an economical method to produce biofuels. The superiority of heterogeneous catalysis promotes the development of bio-based catalysts. Carbon materials prepared from agricultural and forestry biomass waste have good application prospects in catalysis. In the present study, Xanthoceras sorbifolia shell waste was used as the raw material, Xanthoceras sorbifolia Bunge Carbon (XC) was used as the catalyst carrier, and K2CO3 was used as the activator to prepare a heterogeneous catalyst (KXC). The heterogeneous catalyst was characterized by scanning electron microscopy-energy dispersion X-ray spectroscopy (SEM-EDS), Fourier-transform infrared spectroscopy (FTIR), thermogravimetric analysis (TGA), X-ray diffraction (XRD), and Brunauer–Emmett–Teller (BET) and X-ray photoelectron spectroscopy (XPS) analysis techniques to evaluate its chemical composition, structure, and physical morphology. EDS and XPS revealed the presence of K metal, which provided an alkaline site for the transesterification reaction to produce biodiesel. The biodiesel yield was observed by gas chromatography−mass spectrometry (GCMS). Under the reaction conditions of a methanol-to-oil molar ratio of 12:1, a reaction time of 90 min, a temperature of 65 °C, and a catalyst loading of 4 wt.% using 25KXC-600-4, the yield of biodiesel can reach 95.13 ± 0.82%. After being repeated five times, the yield was still 58.11 ± 3.80%. The catalyst has no waste generation, and has the characteristics of simple preparation and environmental friendliness, which make it a green heterogeneous catalyst for biodiesel production.

TiO2-ZnO based nano catalyst for biodiesel production: synthesis, characterisation, performance & emission study

Biodiesel (BD) production from bio-oil in the agriculture-based economy could minimise the energy dependency on fossil diesel (FD). Viscous properties and lower calorific value of BD restrict their direct application in the DE. These properties of BD can be enhanced by using advanced material (catalyst, adhesive etc) along with by modifying BD preparation processes. The present work deals with the synthesis and characterisation of nanocatalyst (TiO2-ZnO) and their application in BD production from waste cooking oil (WCO) via the transesterification process. Catalyst TiO2-ZnO was characterised by XRD, SEM and FTIR analysis. Catalyst TiO2-ZnO in a 4:1 mass ratio indicates the maximum BD yield. Maximum BD yield of 88% was noticed for molar methanol/WCO ratio – 1:1; catalyst dose – 2.5 g/l; reaction time – 120 min at reaction temperature -65°C respectively. The prepared BD was characterised by FTIR, GCMS, and HNMR analysis and compared their result with fossil diesel. Engine performance confirms that the 20% BD containing BM increases BSFC and EGT by 40 and 8.33% and decreases BTE by 14.26% in comparison with FD. But HC and CO emissions decreased by 50.27 and 57.44% respectively. While CO2 and O2 emissions are increased by 2.65 and 4.76% respectively. Highlights A maximum yield of 88% with TiO2-ZnO (4:1) mass ratio was obtained. BSFC and EGT increased by 40 and 8.33%. HC and CO emissions decreased by 50.27% and 57.44%.

Recyclability of Zinc Palmitate-Based Composites in Fatty Acid Methyl Ester Production from Oil Feedstocks at Varied Acidity.

Zinc hydroxide nitrate (Zn5) is one of the layered metal hydroxide materials, which has been extensively reported as an effective bifunctional catalyst for biodiesel production from acidic oils. This report gives a comprehensive summary of the reactivity of Zn5 in the methanolysis of various oil feedstocks, plant oils, free fatty acids, and other acidic oils. Notably, as evidenced by this work, Zn5 is highly effective in converting acidic oils [palmitic acid/palm oil (PO)] to fatty acid methyl ester (FAME or biodiesel) at high yields ranging from 80 to 95%, withstanding acid content up to 10% without soap formation. The high FAME yields result from complex methanolysis and hydrolysis processes, e.g., transesterification of triglycerides in the PO, esterification of palmitic acid, and hydrolysis of the triglycerides. Despite this, Zn5 is nonrecyclable because it is unstable in the reaction media and transforms into zinc hydroxide nitrate/zinc palmitate (Zn5/ZnP) composites. The Zn5/ZnP composites were suitable for use in FAME production from PO at 100 °C for 2 h by using a methanol-to-oil molar ratio of 30:1, yielding high FAME yields of 97 and 70.7% in the first and fourth cycles, respectively. This study added better insight into how to effectively produce FAME from oil feedstocks of varying acidity by using zinc layered hydroxide- or zinc carboxylate-based materials.

Thermal Conversion of Coral Waste and its Utilization as Low-Cost Catalyst for Biodiesel Production

This study investigates the thermal conversion of waste coral and its utilization as a heterogeneous catalyst for biodiesel production from soybean oil. In this work, waste coral is calcined at varied temperatures of 800, 900, and 1000°C, and the effect of the calcination temperature on the physicochemical character of the solid is evaluated through Fourier-transform infrared spectroscopy, X-ray diffraction, scanning electron microscopy, and basicity measurement. The results show that the higher temperature facilitates the conversion of CaCO3 of the aragonite and calcite phases in raw waste coral into CaO, achieving a complete conversion at the temperature of 1000°C. Thermal conversion influences the increased surface basicity of the solid, which is associated with the higher activity for biodiesel production. Further studies on the obtained CaO as a catalyst demonstrate the catalyst dosage and the methanol-to-oil ratio as significant factors for fatty acid methyl ester production. The highest yield of 98.7% is achieved after a 3 hours reaction with 8 wt.% catalyst dosage and 9:1 methanol-to-oil ratio. The catalyst exhibits stability with an insignificantly decreased yield until the fifth usage cycle. The optimum conditions and reusability features of the calcined waste coral suggest that waste coral is a favorable CaO catalyst source for biodiesel production.

Sustainable production of biodiesel from waste cooking oil using magnesium oxide nano catalyst: An optimization study

Biodiesel is rapidly becoming an efficient substitute for fuel and a potentially significant future renewable energy source. In recent years, used cooking oil has been used as a feedstock for biofuel to reduce production costs. Due to its high catalytic activity, low cost, and eco-friendliness, Nano magnesium oxide (MgO) has attracted attention as a catalyst for biodiesel production. Our work presents the preparation of nanomagnesium oxide (MgO) by the sol–gel method, and its characterization. Optimum conditions and the productive combination of waste cooking oil, methanol, and the synthesized nanocatalyst were predicted using response surface methodology. The optimum conditions were methanol to oil ratio of 7:1, temperature of 50 °C and time of 60 min. The expected values for the yield of biodiesel production responses are quite like the actual values, demonstrating the consistency of the models used for establishing a relationship between the independent process variables and the responses. The predicted model's F-value was 9.09 indicating that the model is significant. The model's pure error had a poor correlation, as the "Lack of Fit F-values” 4.16. The quadratic model fits the data well because the R-squared value for the model equation 92%. The expected values for the yield of biodiesel production responses are quite like the actual values, demonstrating the consistency of the models used for establishing a relationship between the independent process variables and the responses. Biodiesel was characterized using gas chromatography–mass spectrometry and Fourier transform infrared spectroscopy.

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.

An economic, and environmentally benign Psidium guajava L. leaves catalyst for biodiesel production at room temperature: Process optimization, and life cycle cost analysis

Biodiesel has emerged as a popular alternative to conventional fossil fuel in transportation sector and thus producing low-cost biodiesel is a topic of interest for a large community of researchers. This study reports the preparation of an efficient and robust heterogeneous catalyst from dried Psidium guajava L. (Guava) leaves and its application towards generation of biodiesel from soybean oil at room temperature. The biomass material was calcinated at variable temperature and the efficiency of each of the catalyst prepared was studied. The catalyst generated as well as the product biodiesel was thoroughly characterized using sophisticated analytical techniques. The catalyst was found to have mesoporous structure with active basic sites which contributed towards accelerating the transesterification process. Detailed characterization unveiled the occurrence of Ca as oxide and carbonate, in addition to a certain quantity of K in oxide and carbonate form, which contribute to the catalyst’s activity. Maximum biodiesel yield of 95.8 % was observed for reaction performed under optimum experimental conditions i.e., 1:17 oil-to-methanol ratio, 6 wt% loading of GL-850 (catalyst prepared by calcination at 850°C), and 15 % n-Hexane loading for 3 h at room temperature. GL-850 demonstrated exceptional recyclability for up to the fifth cycle exhibiting a mere 3.7 % decline in yield. The calculated expense for 1 kg catalyst was found to be $0.478, whereas the production cost of 1 kg biodiesel was found to be merely $1.120, indicating a strong economic feasibility of the process.

MILs as Heterogeneous Catalysts for Biodiesel Production

MILs as Heterogeneous Catalysts for Biodiesel Production

CCD-RSM optimization of biodiesel production from waste cooking oil using Angulyagra oxytropis and Bellamya crassa snail shell-based heterogeneous catalysts

In the present study, labuk tharoi (Angulyagra oxytropis), and ningkhabi tharoi (Bellamya crassa) were utilized to produce CaO catalyst for biodiesel production using waste cooking oil (WCO). The snail shells were calcined at a temperature of 800−1000℃ for 4 h and characterized using XRD, FTIR, BET, SEM, and EDX analysis. Central composite design-response surface methodology (CCD-RSM) was employed, and the input parameters considered for optimization were (i) catalyst calcination temperature (800−1000℃), (ii) methanol: oil ratio (molar) (6:1−12:1), (iii) catalyst loading (3−7 wt.%), and (iv) reaction temperature (55−75℃). A quadratic regression model was aliased by CCD-RSM with R2 values of 0.9291 and 0.976 for waste cooking oil methyl ester-labuk tharoi (WCOME-LT), and waste cooking oil methyl ester-ningkhabi tharoi (WCOME-NT) models indicating a good fit. An optimum biodiesel yield of (95.87, 95.91 %) was obtained at catalyst calcination temperature (891, 886℃), methanol to oil molar ratio (9.89:1, 9.67:1), catalyst loading weight % (7, 7 wt.%), and reaction temperature (75, 75℃) for WCOME-LT and WCOME-NT model respectively. The calcination temperature has a major impact on the biodiesel yield as per analysis of variance. The catalyst reusability was up to four cycles with a biodiesel yield of more than 83 %.

Catalytic Potential of Singgora Roof Tiles in Transesterification for Sustainable Biodiesel

The study centred around the uitilization of Singgora roof tiles as a heterogeneous catalyst in the production of biodiesel via the transesterification process. The motivation behind this choice stems from the non-recyclable nature of Singgora roof tiles and their potential applicability in biodiesel synthesis. To enhance the catalytic properties, zinc oxide (ZnO) is incorporated using the wet impregnation technique during catalyst preparation. The catalyst was characterized by XRF and SEM-EDX. A two-step transesterification method is employed to mitigate the levels of free fatty acid (FFA) in waste cooking oil (WCO). The initial step involves treating the WCO with sulfuric acid (H2SO4) to reduce FFA. Subsequently, the Singgora roof tiles catalyst is utilized in the second step. A high yield of FAMEs, specifically 96.96%, was achieved under the optimal conditions, which included a methanol-to- oil ratio of 12:1, a catalyst concentration of 1 wt.%, a reaction temperature of 65 °C, and a reaction time of 2 hours. The quality of the biodiesel produced was analyzed according to biodiesel standards such as ASTM D6751, EN 14214, and AOCS, and it met all the required standards. The study demonstrates the potential of using Singgora roof tiles as a heterogeneous catalyst in biodiesel production, offering a promising approach to repurposing non-recyclable materials and advancing sustainable biodiesel production methods.

Influence of carbon template and ultrasound irradiation on combustion design of nanostructured calcium manganese oxides used in biodiesel production

Biodiesel, derived from renewable biomass, serves as a sustainable alternative to diesel produced from fossil fuels. This study explores the use of nanostructured MgO/Ca2Mn3O8 catalysts for biodiesel production through transesterification. Ca2Mn3O8 was synthesized as a support catalyst via combustion synthesis, employing carbon templates to control pore size. MgO was impregnated as the active phase using ultrasonic irradiation to enhance particle dispersion. Various characterization techniques, including XRD, FESEM, AFM, TEM, EDX, BET-BJH, and TPD-CO2, were utilized to analyse morphology, porosity, basicity, and active phase dispersion. The use of carbon templates increased pore diameters compared to catalysts without templates, while ultrasonic irradiation improved MgO dispersion. The MgO/Ca2Mn3O8 catalyst with a 10 wt% carbon template and ultrasonic irradiation achieved a maximum conversion rate of 95.5%. Its mesoporous structure, resembling a sponge, facilitated triglyceride diffusion. Stability tests indicated a 90% conversion rate after five reuses. The nanostructured MgO/Ca2Mn3O8 catalyst, with its tailored porosity and structure, demonstrated excellent performance in biodiesel production. Systematically adjusting support porosity and active site dispersion provides a viable approach for designing effective heterogeneous catalysts.

Effectiveness of empty fruit bunch ash as the catalyst for palm oil transesterification

Empty Fruit Bunch (EFB) resulted from oil palm plantations and mills can be converted into ash through open combustion. The EFB ash then treated by simple calcination and used as a heterogeneous catalyst for biodiesel production. The characteristics of EFB ash were identified based on its elemental composition, porous structure, and active site size. The effectivity of the EFB ash as a catalyst was tested in a transesterification reaction of Refined Bleached Deodorized Palm Oil (RBDPO) with excess methanol (30 %-w) in various catalyst loads (in%-wt). The lab-scale experiments were conducted in a three-neck glass reactor, which was put on the hot plate stirrer at 450 rpm. The EFB ash performed the best as a catalyst by attaining optimal conversion at 65 °C for 1 h with a 16 %-wt of catalyst load. In this condition, most of the standard quality of biodiesel were complied with total glycerol under 0.24% and ester methyl contents up to 98.9 %. The characteristics tests showed that the properties and active side of the EFB ash are excellent after calcination at 600 for 5 h. The recyclability test of EFB ash as a catalyst showed high performance in two repetition cycles, each showing an increase in the yield of biodiesel, which was 92.21 % in cycle 2 and 91.23 % in cycle 3.

Use of biochar as a catalyst for biodiesel production

The economic viability of biodiesel (BD) production is highly dependent on conversion techniques using inexpensive oil feedstocks. In this study, BD was synthesised by the thermally induced (non-catalytic) transesterification of oil extracted from camellia seed (42.23 wt% lipid content). The BD yield from the non-catalytic transesterification of camellia oil was higher than that from the alkali-catalysed process. The BD yield from the alkali-catalysed transesterification of camellia oil for 60 min was 84.1 wt%, whereas that from the non-catalytic process for ≤ 1 min at 360 ˚C was 93.5 wt%. To realise a virtuous circle in the production of BD, this study sought a strategic way to valorise oil-extracted biomass waste (lignocellulose-based). Specifically, this study sought a method for valorising biochar as an effective catalyst, hypothesizing that earth alkaline metals finely dispersed within the porous structure of biochar would effectively enhance catalytic capability. The BD yield in the presence of camellia biochar was 92.4 wt% (saturated at ≥ 240 ˚C). Thus, the reaction kinetics for the transesterification of camellia oil over camellia biochar was catalytically accelerated. Such efforts provide opportunities to enhance economic viability and realise the concept of a sustainable cycle in BD production.

Microwave absorbing alkaline catalyst for biodiesel production via MIL-100(Fe): Catalytic optimization, characterizations, kinetics, and distillation simulation

Microwave heating (MW) is known for its efficacy in promoting transesterification for biodiesel production. However, the microwave-induced catalysis, linked to catalyst absorbing capability, remains poorly understood. Herein, a class of alkaline catalysts with strong microwave absorption were synthesized, validating their positive impact on transesterification. Various methods were used to reveal the relationship between microwave absorbing capacity and physicochemical properties of the synthesized catalyst (KF/Mg-MIL). Results indicated the previously recognized basicity’s role for KF/Mg-MIL was surpassed by microwave absorbing capability (permittivity and permeability) in MW (2.45 GHz). KF/Mg-MIL, with εr = 4.94′-j1.09″ and μr = 1.03′-j0.024″, efficiently transformed microwave into thermal energy via the dielectric loss and magnetic loss, saving 50 % energy consumption and reducing 1051.61 kg CO2 for per ton biodiesel compared to water bath heating (WB). Notably, “non-thermal” effect was observed with KF/Mg-MIL in MW, which reduced activation energy by 2.49 kJ/mol and increased the frequency factor by 793.32 min−1 in comparison to WB.

Synthesis and evaluation of CuO/UiO-66 metal-organic frameworks as a solid catalyst for biodiesel production from waste cooking oil

Metal-organic frameworks (MOFs) are excellent for immobilizing guest active species due to their high surface area and porosity. In this study, CuO/UiO-66 catalysts with varying amounts of CuO were successfully synthesized and used for converting waste cooking oil (WCO) to biodiesel. The catalysts were characterized using N2 adsorption-desorption, XRD, NH3-TPD, SEM, TEM, TGA and FTIR. The biodiesel was characterized using NMR and GC–MS. The results showed that CuO/UiO-66 displayed high catalytic activity due to the synergistic effect between UiO-66 and copper oxide in the composite. Under optimum reaction conditions, we achieved a 90.1 % conversion with the 7 %CuO/UiO-66 catalyst. This catalyst also displayed good stability and reusability with a conversion of 81.06 % after three cycles. Our kinetic studies revealed a pseudo-first-order kinetics, with 32.26 kJ/mol in activation energy, consistent with a chemically controlled reaction.

Biodiesel synthesis via heterogeneous catalysis: investigation of the catalytic performance of CLV98/900 on quality and yield at different production scales

This article investigated the obtaining of fatty acid alkyl esters (FAAE) from waste cooking oil (WCO) via heterogeneous catalysis, applying a catalyst based on mixed oxides (Na-FeAlO) from the red mud (RM) sintering process with sodium carbonate, which was called CLV98/900. The synthesized catalyst was characterized by thermogravimetric analysis, differential thermogravimetry and differential calorimetric analysis (TG/DTG and DSC), Raman spectroscopy, and specific surface area (BET). The influence of the operational parameters oil/alcohol molar ratio (1:15 and 1:45), reaction time (60, 120 and 180 min) and scale-up on the yield and conversion of the reaction into biodiesel produced were investigated. The catalyst characterization indicated an efficient microstructural transformation of the red mud, thermal stability at the study temperature of 70 ºC, and a mesoporous characteristic. The best yield and reaction conversion results were obtained with the parameters: oil/ethanol ratio of 1:15, 70 °C, 1% catalyst and 60 min, achieving yield and conversion of approximately 75%. The formation of biodiesel was confirmed by GC-MS analysis, reaching a maximum of 100% conversion to the lower phase obtained after the purification process. Therefore, CLV98/900 becomes a promising option when used as a catalyst in biodiesel production through the transesterification reaction of WCO.

A Spherical Superhydrophobic Activated Carbon Catalyst for Biodiesel Production ‐Exploring Process Efficiency, Kinetics, Thermodynamics and Life Cycle Cost Analysis

AbstractEngineering the wettability of functional materials holds significant interest, focusing on the need for superhydrophobic catalysts, crucial for their ability to prevent the poisoning of active sites by water, produced in situ or as a by‐product. Herein, for the first time, a superhydrophobic spherical activated carbon (SSAC@PhSO3H) is engineered as a catalyst via a novel synthetic approach and tailored in Jatropha curcas oil (JCO) biodiesel synthesis. With a large surface area (1461 m2 g−1), high acid density (6.26 mmol g−1), and water contact angle (163.4°), the catalyst demonstrates superior performance and remarkable water repellency, firmly establishing its superhydrophobic characteristics. Response Surface Methodology based on the Central Composite Design (RSM‐CCD) approach predicted a maximal biodiesel yield of 98.8% (80 °C, 5 wt%, 15:1 methanol to oil molar ratio (MOMR), and 40 min). Life cycle cost analysis (LCCA) estimates biodiesel production cost of 0.37 USD ($) per kg emphasizing high commercial viability. Compared with H2SO4‐sulfonated biochar, SSAC@PhSO3H retains its inherent activity (86.8 ± 0.4% yield in 10th run) and spherical morphology even after nine successive reaction cycles indicating high stability. Nevertheless, JCO biodiesel's fuel properties met European Norm, EN 14 212 and American Society for Testing and Materials, ASTM D6757 standards, highlighting its potential for industrial biodiesel production.

Hybrid CaO/ZnFe2O4 Modified with Al2O3 as a Green Catalyst for Biodiesel Production from Waste Cooking Oil

In this work, biodiesel was produced from waste cooking oil (WCO) via a green catalyst of CaO-ZnFe2O4 modified Al2O3. The catalyst was characterized using Fourier-transform infrared spectroscopy (FTIR), X-ray powder diffraction (XRD), scanning electron microscopy (SEM), energy dispersive x-ray (EDX), SEM-mapping, Brunauer-Emmett-Teller (BET), transmission electron microscopy (TEM) analyses. The catalyst performance was studied in the transesterification reaction of WCO conversion to biodiesel. The catalytic activity increased with the combination of nanoparticles effect and support catalysts obtained biodiesel yield of nano-Al2O3, nano-CaO, ZnFe2O4, CaO-ZnFe2O4, and CaO-ZnFe2O4/Al2O3 is 36.86%, 67.16%, 74.83%, 86.54%, and 93.41%, respectively. The best biodiesel yield was 93.41% with a mass ratio of Al2O3 to CaO-ZnFe2O4 (2:1). The physicochemical properties (acid number, density, kinematic viscosity, flash point, and cetane number) of biodiesel under the optimal conditions agreed with the ASTM standard. These results show that the developed nanocomposite has great potential to reduce biodiesel production costs because derived from WCO. In conclusion, CaO-ZnFe2O4 modified Al2O3 as a catalyst has a high potential for biodiesel production on a large scale.

Concise Review on Integral Structure of Egg Shell Membrane

The article outlines various valuable applications for eggshell waste, including its use as a catalyst in biodiesel production to minimize pollutants, as an absorbent for heavy metals in wastewater, as a biomaterial for bone tissue replacement, and as a fertilizer and calcium supplement in various domains. It highlights the increasing research interest in exploring these applications for eggshell waste. This highlights the potential of the eggshell membrane (ESM) as a biomaterial for wound dressing due to its abundant availability and favourable properties. The study developed an extraction protocol for ESM and evaluated its physical, chemical, mechanical, and biological properties for wound dressing applications. Results showed that ESM retained its structure and composition after extraction, with promising characteristics such as optical transparency, porosity, fluid absorption, thermal stability, and mechanical strength. Biological studies confirmed its excellent biocompatibility with corneal cells, suggesting its potential for ophthalmic wound treatment and other biomedical applications, contributing to sustainable biomaterial development. The article discusses the formation and mineralization of calcareous eggs, primarily focusing on studies of chicken eggshells. It highlights areas of uncertainty such as the role of amorphous calcium carbonate and the molecules involved in eggshell formation. Additionally, it mentions the recent advancements in avian genomics and proteomics, which will aid in comparative studies of egg shell constituents across different bird species.