scholarly journals Production and Characterization of Biodiesel from Avocado Peel Oils using Experimental Analysis (ANOVA)

2021 ◽  
pp. 104-111
Author(s):  
Tafere Aga Bullo ◽  
Feyissa Bekele Fana
Keyword(s):  
Reaction Temperature ◽  
Alternative Energy ◽  
Cetane Number ◽  
Diesel Oil ◽  
International Standards ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Optimum Process ◽  
Minimal Amount

The crisis of energy due to the increasing awareness of the depletion of fossil fuel resources, biodiesel is an alternative energy source and promising potential energy that grows rapidly, due to its high contribution to the environment friendly, renewable, non-toxicity, biodegradability, essentially sulfur-free, and as a strategical source of renewable energy in substitution to diesel oil and contributes a minimal amount of net greenhouse gases. In this study, the extracted oil used for biodiesel production from waste avocado peel was investigated in a laboratory approach. Experimental results evaluate the major optimum process parameters for base-catalyzed transesterification on biodiesel yield as well as its properties. The most important variables affecting methyl ester yield during the transesterification reaction are the molar ratio of alcohol to oil and the reaction temperature. A 95.2% FAME conversion was obtained using a methanol/oil ratio of 6:1, 1.21g NaOH, reaction time 67.5 min, and 60 0C reaction temperature. Important properties of (characterization) produced biodiesel are, (pHof 7.8, specific gravity of 0.88, density at 15 0C, kg/m3, the kinematic viscosity of biodiesel was found to be 4.22 m 2·s −1 at 40 0C, the flashpoint was 161 0C and Cetane number of 49 are well-matched the relevant international standards for biodiesel quality produced.  This result shows that the oil obtained from avocado peel can be used for biodiesel production as an alternative fuel as compared to those of ASTM and EN standards.

scholarly journals Biodiesel Production from Rubber Seed Oil via Esterification Process

2012 ◽  
Vol 1 (2) ◽  
pp. 57-60 ◽  
Author(s):  
Widayat Widayat ◽  
S Suherman
Keyword(s):  
Alternative Energy ◽  
Seed Oil ◽  
Raw Materials ◽  
Free Fatty Acid Level ◽  
Diesel Oil ◽  
Biodiesel Production ◽  
Rubber Seed Oil ◽  
Rubber Seed ◽  
Product Characterization

One promise source of alternative energy is biodiesel from rubber seed oil, because the raw materials available in plentiful quantities and can be renewed. In addition, the rubber seed is still lack of utilization, and Indonesia is one of the largest rubbers producing country in the world. The objective of this research is to studied on biodiesel production by esterification process. Parameters used in this study are the ratio of catalyst and temperature and its influence on the characteristics of the resulting biodiesel product. Characterization of rubber seed include acid content number analysis, saponification numbers, density, viscosity, iodine number, type of free fatty acids and triglyceride oils. The results of analysis showed that rubber seed oil content obtained is 50.5%. The results of the GCMS analysis showed that a free fatty acid level in rubber seed is very high. Conversion into bio-diesel oil is obtained by at most 59.91% and lowest 48.24%.

scholarly journals Response Surface Optimization of Biodiesel Production from Nyamplung (Calophyllum inophyllum) Oil Enhanced by Microwave and Ionic liquid + NaOH Catalyst

2019 ◽  
Author(s):  
Prima Astuti Handayani ◽  
Abdullah Abdullah ◽  
Hadiyanto Hadiyanto
Keyword(s):  
Ionic Liquid ◽  
Response Surface ◽  
Reaction Temperature ◽  
Catalyst Concentration ◽  
Process Condition ◽  
Raw Material ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Optimum Process ◽  
Calophyllum Inophyllum

Nyamplung (Calophyllum inophyllum) plant is a highly potential raw material in the biodiesel production, the oil in the seeds is 50-73 %. The microwave has been intensively applied to reduce the processing time while ionic liquid also was used as an acceleration agent in the biodiesel production. The optimum process condition of the biodiesel production using Ionic liquid + NaOH as a catalyst mixture and assisted with microwave heating system were determined in this study. Response Surface Methodology (RSM) was used to optimize three transesterification reaction variables: the catalyst concentration of (0.5-1.5 %wt), the reaction temperature of 60-80 oC, and methanol to oil molar ratio of 6:1–12:1, while the transesterification time was set constant at 6 minutes. The optimization showed that the maximum biodiesel yield can be obtained was 95.8 % at the catalyst concentration of 1.2 %wt, the reaction temperature of 71.3 oC, and methanol to oil molar ratio of 10.8 mole/mole.

scholarly journals TRANSESTERIFICATION OF PALM OIL USING THE TiO2/nano-MONMORILLORITE (nano-MMT) COMPOSITE CATALYST FROM ACEH TAMIANG BENTONITE IN THE PRODUCTION OF BIODIESEL

2021 ◽  
Vol 13 (1) ◽  
pp. 19-24
Author(s):  
Teuku Andi Fadlly ◽  
Ida Ratna Nila ◽  
Nirmala Sari
Keyword(s):  
Palm Oil ◽  
Alternative Energy ◽  
Fossil Fuels ◽  
Acid Methyl Ester ◽  
Diesel Oil ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Composite Catalyst ◽  
Solid State Method ◽  
Animal Fats

Transesterification of palm oil using a TiO2/nano-Monmorillorite (nano-MMT) composite catalyst from Aceh Tamiang bentonite in Biodiesel production has been carried out. Biodiesel is bioenergy obtained from vegetable oils, animal fats, microorganisms, and plants. This is alternative energy to replace fossil fuels, especially diesel oil. Biodiesel is proven to be more environmentally friendly in reducing hydrocarbon and sulfur emissions. In this study, TiO2 will be composited with nano-MMT using the solid-state method and analyzed using XRD. Both of these materials are used as catalysts for biodiesel production. The transesterification process will be used in the production of biodiesel, where the molar ratio of palm oil to methanol is 1:12. TiO2/nano-MMT composite catalyst will be varied (2 and 4 grams). Biodiesel samples will be analyzed using GC-MS. The results obtained show that the TiO2/nano-MMT composite catalyst from Aceh Tamiang bentonite can convert Fatty Acid Methyl Ester (FAME) from palm oil. The 2 grams of the composite catalyst produced biodiesel of 89.38% and 4 grams of 64.88%.

Ultrasonic-Assisted Biodiesel Production from Palm Oil Using Adsorption of Homogeneous Catalysts over Solid Sodium Silicate

2013 ◽  
Vol 781-784 ◽  
pp. 2396-2399
Author(s):  
Passawron Krongtanin ◽  
Anurak Petiraksakul
Keyword(s):  
Reaction Temperature ◽  
Palm Oil ◽  
Alternative Energy ◽  
Heterogeneous Catalysts ◽  
Filter Cake ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Catalyst Recycle ◽  
Ultrasonic Assisted ◽  
Alternative Energy Resources

Biodiesel is an alternative energy resources, which produced from transesterification of oils and alcohols using homogeneous and heterogeneous catalysts. Ultrasonic was used as pre-mixer for KOH, Na2SiO3, palm oil and methanol before increasing the reaction temperature to 60°C using a water bath. All experiments were conducted at a molar ratio of methanol:oil of 6:1, reaction time of 60 min, reaction temperature of 60C and well mixing. The suspension was filtered after the end of the reaction. Purified biodiesel was obtained by water washing processes after crude biodiesel was separated from glycerol by 2 hr standing in a separating funnel. Filter solid cake was instantly used as supporter in next batch of the reaction. Effects of four variables, namely, pre-mixing period in the range of 0-10 s, number of filter cake recycle (2-4 cycles), sonicator power (10-90% of max. power of 200 watt and 20 kHz) and amount of KOH addition (0.25-0.75 g) were investigated. Response surface methodology was employed to evaluate and optimize the biodiesel production processes using Na2SiO3adsorbed with KOH as catalyst. The design of experiment was carried out using the MINITAB RELEASE 16 and a result of 31 experiments was suggested to be made. The result showed the optimum condition of pre-mixing period of 14 s, the number of catalyst recycle to be 2 cycle, sonicator power of 36.3%and KOH addition of 0.3 g.

Mango (Magnifera indica) seed oil grown in Dilla town as potential raw material for biodiesel production using NaOH- a homogeneous catalyst

2019 ◽  
Author(s):  
Chem Int
Keyword(s):  
Diesel Engine ◽  
Physicochemical Properties ◽  
Seed Oil ◽  
Methyl Esters ◽  
Pollution Prevention ◽  
Raw Material ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Homogeneous Catalyst ◽  
Minimal Amount

Biodiesel produced by transesterification process from vegetable oils or animal fats is viewed as a promising renewable energy source. Now a day’s diminishing of petroleum reserves in the ground and increasing environmental pollution prevention and regulations have made searching for renewable oxygenated energy sources from biomasses. Biodiesel is non-toxic, renewable, biodegradable, environmentally benign, energy efficient and diesel substituent fuel used in diesel engine which contributes minimal amount of global warming gases such as CO, CO2, SO2, NOX, unburned hydrocarbons, and particulate matters. The chemical composition of the biodiesel was examined by help of GC-MS and five fatty acid methyl esters such as methyl palmitate, methyl stearate, methyl oleate, methyl linoleate and methyl linoleneate were identified. The variables that affect the amount of biodiesel such as methanol/oil molar ratio, mass weight of catalyst and temperature were studied. In addition to this the physicochemical properties of the biodiesel such as (density, kinematic viscosity, iodine value high heating value, flash point, acidic value, saponification value, carbon residue, peroxide value and ester content) were determined and its corresponding values were 87 Kg/m3, 5.63 Mm2/s, 39.56 g I/100g oil, 42.22 MJ/Kg, 132oC, 0.12 mgKOH/g, 209.72 mgKOH/g, 0.04%wt, 12.63 meq/kg, and 92.67 wt% respectively. The results of the present study showed that all physicochemical properties lie within the ASTM and EN biodiesel standards. Therefore, mango seed oil methyl ester could be used as an alternative to diesel engine.

scholarly journals Continuous Integrated Process of Biodiesel Production and Purification—The End of the Conventional Two-Stage Batch Process?

Energies ◽  
2021 ◽  
Vol 14 (2) ◽  
pp. 403
Author(s):  
Matea Bačić ◽  
Anabela Ljubić ◽  
Martin Gojun ◽  
Anita Šalić ◽  
Ana Jurinjak Tušek ◽  
...  
Keyword(s):  
Extraction Efficiency ◽  
Deep Eutectic Solvent ◽  
International Standards ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Process Conditions ◽  
Integrated Process ◽  
Free Glycerol ◽  
Mass Ratio ◽  
Glycerol Content

In this research, optimization of the integrated biodiesel production process composed of transesterification of edible sunflower oil, catalyzed by commercial lipase, with simultaneous extraction of glycerol from the reaction mixture was performed. Deep eutectic solvents (DESs) were used in this integrated process as the reaction and extraction media. For two systems, choline chloride:glycerol (ChCl:Gly) and choline chloride:ethylene glycol (ChCl:EG), respectively, the optimal water content, mass ratio of the phase containing the mixture of reactants (oil and methanol) with an enzyme and a DES phase (mass ratio of phases), and the molar ratio of deep eutectic solvent constituents were determined using response surface methodology (RSM). Experiments performed with ChCl:Gly resulted in a higher biodiesel yield and higher glycerol extraction efficiency, namely, a mass ratio of phases of 1:1, a mass fraction of water of 6.6%, and a molar ratio of the ChCl:Gly of 1:3.5 were determined to be the optimal process conditions. When the reaction was performed in a batch reactor under the optimal conditions, the process resulted in a 43.54 ± 0.2% yield and 99.54 ± 0.19% glycerol extraction efficiency (t = 2 h). Unfortunately, the free glycerol content was higher than the one defined by international standards (wG > 0.02%); therefore, the process was performed in a microsystem to enhance the mass transfer. Gaining the same yield and free glycerol content below the standards (wG = 0.0019 ± 0.003%), the microsystem proved to be a good direction for future process optimization.

scholarly journals Biodiesel Production from Melia azedarach and Ricinus communis Oil by Transesterification Process

Catalysts ◽  
2020 ◽  
Vol 10 (4) ◽  
pp. 427 ◽  
Author(s):  
Muhammad Awais ◽  
Sa’ed A Musmar ◽  
Faryal Kabir ◽  
Iram Batool ◽  
Muhammad Asif Rasheed ◽  
...  
Keyword(s):  
Ricinus Communis ◽  
Cost Effective ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Melia Azedarach ◽  
Renewable Fuel ◽  
Animal Fats ◽  
Edible Crops ◽  
American Society

Biodiesel is a renewable fuel usually produced from vegetable oils and animal fats. This study investigates the extraction of oil and its conversion into biodiesel by base-catalyzed transesterification. Firstly, the effect of various solvents (methanol, n-hexane, chloroform, di-ethyl ether) on extraction of oil from non-edible crops, such as R. communis and M. azedarach, were examined. It was observed that a higher concentration of oil was obtained from R. communis (43.6%) as compared to M. azedarach (35.6%) by using methanol and n-hexane, respectively. The extracted oils were subjected to NaOH (1%) catalyzed transesterification by analyzing the effect of oil/methanol molar ratio (1:4, 1:6, 1:8 and 1:10) and varying temperature (20, 40, 60 and 80 °C) for 2.5 h of reaction time. M. azedarach yielded 88% and R. communis yielded 93% biodiesel in 1:6 and 1:8 molar concentrations at ambient temperature whereas, 60 °C was selected as an optimum temperature, giving 90% (M. azedarach) and 94% (R. communis) biodiesel. The extracted oil and biodiesel were characterized for various parameters and most of the properties fulfilled the American Society for Testing and Materials (ASTM) standard biodiesel. The further characterization of fatty acids was done by Gas Chromatography/Mass Spectrometer (GC/MS) and oleic acid was found to be dominant in M. azedarach (61.5%) and R. communis contained ricinoleic acid (75.53%). Furthermore, the functional groups were analyzed by Fourier Transform Infrared Spectroscopy. The results suggested that both of the oils are easily available and can be used for commercial biodiesel production at a cost-effective scale.

scholarly journals Box-Behnken Design for Optimization on Biodiesel Production from Palm Oil and Methyl Acetate using Ultrasound Assisted Interesterification Method

2021 ◽  
Author(s):  
Mahfud Mahfud ◽  
Ansori Ansori
Keyword(s):  
Palm Oil ◽  
Energy Demand ◽  
Alternative Energy ◽  
Methyl Acetate ◽  
Catalyst Concentration ◽  
Separation Process ◽  
Operating Conditions ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Box Behnken Design

Energy demand is currently increasing in line with technological and economic developments, but not accompanied by an increase in energy reserves. So we need another alternative energy that can be renewed, namely biodiesel. Biodiesel has been produced commercially through the transesterification from vegetable oil with methanol using catalyst that produces esters and glycerol. The formation of glycerol which is by-product can reduce its economic value, so it needs to be done the separation process. Therefore, a new route is proposed in this study, namely the interesterification reaction (non-alcoholic route) using methyl acetate as an alkyl group supplier and potassium methoxide catalyst. The superiority of the product produced by the interesterification reaction is biodiesel with triacetin byproducts which have an economical value and can be added to biodiesel formulations because of their solubility so that no side product separation process is needed. To increase the yield of biodiesel and the interesterification rate, the ultrasound method was used in this study. To optimize the factors that affect the interesterification reaction (molar ratio of methyl acetate to oil, catalyst concentration, temperature, and interesterification time), the Box-Behnken design (BBD) is used. Optimal operating conditions to produce the yields of biodiesel of 98.64 % are at molar ratio of methyl acetate to palm oil of 18.74, catalyst concentration of 1.24 %, temperature of 57.84 °C, and interesterification time of 12.69 minutes.

scholarly journals Triethanolamine as an efficient cosolvent for biodiesel production by CaO-catalyzed sunflower oil ethanolysis: An optimization study

2019 ◽  
Vol 73 (6) ◽  
pp. 351-362 ◽  
Author(s):  
Dusica Djokic-Stojanovic ◽  
Zoran Todorovic ◽  
Dragan Troter ◽  
Olivera Stamenkovic ◽  
Ljiljana Veselinovic ◽  
...  
Keyword(s):  
Reaction Temperature ◽  
Sunflower Oil ◽  
Acid Ethyl Ester ◽  
Fatty Acid Ethyl Ester ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Calcium Leaching ◽  
Stirred Reactor ◽  
Optimization Study ◽  
Purification Stage

Triethanolamine was applied as an efficient ?green? cosolvent for biodiesel production by CaO-catalyzed ethanolysis of sunflower oil. The reaction was conducted in a batch stirred reactor and optimized with respect to the reaction temperature (61.6-78.4?C), the ethanol-to-oil molar ratio (7:1-17:1) and the cosolvent loading (3-36 % of the oil weight) by using a rotatable central composite design (RCCD) combined with the response surface methodology (RSM). The optimal reaction conditions were found to be: the ethanol-to-oil molar ratio of 9:1, the reaction temperature of 75?C and the cosolvent loading of 30 % to oil weight, which resulted in the predicted and actual fatty acid ethyl ester (FAEE) contents of 98.8 % and 97.9?1.3 %, respectively, achieved within only 20 min of the reaction. Also, high FAEE contents were obtained with expired sunflower oil, hempseed oil and waste lard. X-ray diffraction analysis (XRD) was used to understand the changes in the CaO phase. The CaO catalyst can be used without any treatment in two consecutive cycles. Due to the calcium leaching into the product, an additional purification stage must be included in the overall process.

Production of Biodiesel from Cooking Oil Using CaO Catalyst

2015 ◽  
Vol 1113 ◽  
pp. 518-522 ◽  
Author(s):  
Mardhiah Mohamad ◽  
Norzita Ngadi ◽  
Nurul Saadiah Lani
Keyword(s):  
Surface Area ◽  
Calcium Oxide ◽  
Reaction Temperature ◽  
Test Method ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Catalyst Amount ◽  
Cooking Oil ◽  
Transesterification Method ◽  
Percentage Conversion

Transesterification method was carried out in biodiesel production from cooking oil (CO). Calcium oxide (CaO) was selected as the best catalyst. This study investigated the effects of percentage conversion of oil to biodiesel from methanol to oil molar ratio and catalyst amount. Brunauer, Emmett and Teller (BET) test method was used to analyze the surface area. The results obtained showed that using 200°C calcined CaO catalyst, 76.67 % biodiesel was successfully converted from oil. This indicates that the cooking oil (CO) has potential to become a future source of biodiesel. 0.5 w/w% catalyst dosages, 3:5 oil to methanol molar ratio and 65°C reaction temperature are the best condition for the biodiesel conversion from oil. This study also shows that conversion of cooking oil is significantly affected by methanol to oil molar ratio and catalyst amount.

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