scholarly journals Preliminary Study on the Use of Biodiesel Obtained from Waste Vegetable Oils for Blending with Hydrotreated Kerosene Fossil Fuel Using Calcium Oxide (CaO) from Natural Waste Materials as Heterogeneous Catalyst

Energies ◽  
2019 ◽  
Vol 12 (22) ◽  
pp. 4306
Author(s):  
S. Ozkan ◽  
J. F. Puna ◽  
J. F. Gomes ◽  
T. Cabrita ◽  
J. V. Palmeira ◽  
...  
Keyword(s):  
Heterogeneous Catalyst ◽  
Liquid Waste ◽  
Reaction Times ◽  
Acid Methyl Ester ◽  
Jet Fuel ◽  
Molar Ratio ◽  
Weight Content ◽  
Waste Cooking Oils ◽  
Waste Shell ◽  
Cooking Oils

In this experimental work, calcium from natural seafood wastes was used as a heterogeneous catalyst separately or in a blend of “shell mix” for producing biodiesel. Several chemical reaction runs were conducted at varied reaction times ranging from 30 min to 8 h, at 60 °C, with a mass content of 5% (Wcat./Woil) and a methanol/oil molar ratio of 12. After the purification process, the biodiesel with fatty acid methyl ester (FAME) weight content measured was higher than 99%, which indicated that it was a pure biodiesel. This work also showed that the inorganic solid waste shell mixture used as the heterogeneous catalyst can be reused three times and the reused mixture still resulted in a FAME content higher than 99%. After 40 different transesterification reactions were performed using liquid (waste cooking oils) and solid (calcium seafood shells) wastes for producing biodiesel, under the specific conditions stated above, we found a successful, innovative, and promising way to produce biodiesel. In addition, blends prepared with jet fuel A1 and biodiesel were recorded with no invalid results after certain tests, at 25 °C. In this case, except for the 10% blend, the added biodiesel had no significant effect on the viscosity (fluidity) of the biojet fuel.

scholarly journals Production of biodiesel by esterification and transesterification from waste cooking oils

2020 ◽  
Vol 38 (1) ◽  
pp. 105-127
Author(s):  
Elsy Arenas ◽  
Aidin Urribarrí ◽  
John Sánchez ◽  
Marisela Rincón ◽  
Karina Martínez ◽  
...  
Keyword(s):  
Fatty Acids ◽  
Free Fatty Acids ◽  
Fast Food ◽  
Methyl Esters ◽  
Reaction Times ◽  
Molar Ratio ◽  
Reaction Conditions ◽  
Waste Cooking Oils ◽  
Hcl Concentration ◽  
Cooking Oils

Large quantities of used vegetable oils (AVUs) are generated annually, as a result of food preparation, which can cause contamination of waters and soils, if they are not disposed of properly, but in turn have great potential in the production of biodiesel. In this work, the AVU collected from fast food establishments were subjected to an esterification pretreatment, varying the reaction conditions, molar ratio, catalyst concentration and time, to decrease the content of free fatty acids generated in the frying processes; after an alkaline transesterification. The initial acidity of the AVUs (10,08 ± 0,22 %) was found to drop below 1 % during esterification at 60 °C and 100 rpm, with RMAVU:MeOH of 1: 7 and HCl concentration of 0.3 % v/v, with a conversion of free fatty acids (FFA) to methyl esters of 94.48 and 98.61 % for reaction times of 4 and 6 hours, respectively. The previously esterified AVUs were subjected to a transesterification process with KOH as a catalyst in the presence of methanol, at 60 °C and 100 rpm, finding that the biodiesel produced was a mixture composed of the methyl esters of linoleic acids (57 %), palmitic (14 %), oleic (22 %), stearic (4 %) and elaidic (3 %). The highest concentration of methyl esters (93,797 ± 0.685 g.L-1) was obtained when using the esterified AVU during 6 hours of reaction. FTIR spectra confirmed the conversion of fatty acids to methyl esters, so this product could be used as a biofuel.

Optimization of Biodiesel Production from Transesterification of Waste Cooking Oils Using Alkaline Catalysts

2014 ◽  
Vol 695 ◽  
pp. 289-292
Author(s):  
M.M. Zamberi ◽  
Farid Nasir Ani ◽  
S.N.H. Hassan
Keyword(s):  
Reaction Time ◽  
Catalyst Concentration ◽  
Acid Methyl Ester ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Waste Vegetable Oil ◽  
Waste Cooking Oils ◽  
Level 3 ◽  
Cooking Oils ◽  
Full Factorial

The transesterification of waste vegetable oil (WVO) with methanol in the presence of potassium hydroxide (KOH) is studied in order to produce biodiesel. All the results were evaluated using central composite design by applying a double 5 level 3 factor full factorial designs. Twenty experiments were replicated under the typical range of parameter conditions coded as x1 for oil molar ratio, x2 as catalyst concentration and x3 for reaction time. The experimental fatty acid methyl ester (FAME) are compared with the predicted FAME using RSM. The optimal predicted FAME production was obtained at 92.60%. It is specified under conditions of molar ratio 4:1 mol/mol, 0.5033 wt% catalyst concentration and reaction time of 60 minutes.

Efficient synthesis of pyrido[2,3-d]pyrimidine-7-carboxylic acids catalyzed by a TiO2/SiO2 nanocomposite in aqueous media at room temperature

2018 ◽  
Vol 73 (9) ◽  
pp. 641-645 ◽  
Author(s):  
Sepehr Sadegh-Samiei ◽  
Shahrzad Abdolmohammadi
Keyword(s):  
Heterogeneous Catalyst ◽  
Carboxylic Acids ◽  
Room Temperature ◽  
Aqueous Media ◽  
Reaction Times ◽  
Molar Ratio ◽  
Efficient Synthesis ◽  
Reaction Conditions ◽  
Moderate Reaction ◽  
Recyclable Heterogeneous Catalyst

AbstractA novel and efficient synthesis of eight 5-aryl-1,3-dimethyl-2,4-dioxo-1,2,3,4,5,8-hexahydropyrido[2,3-d]pyrimidine-7-carboxylic acids using a TiO2/SiO2 nanocomposite with a molar ratio of 1:1 as a recyclable heterogeneous catalyst is described. The desired products, five of which are new, are formed in short reaction times (2–3 h) with high to excellent yields (94%–98%) under very moderate reaction conditions (room temperature, aqueous media).

scholarly journals Comparative study of properties and fatty acid composition of some neat vegetable oils and waste cooking oils

2019 ◽  
Vol 14 (3) ◽  
pp. 417-425 ◽  
Author(s):  
Omojola Awogbemi ◽  
Emmanuel Idoko Onuh ◽  
Freddie L Inambao
Keyword(s):  
Fatty Acid ◽  
Vegetable Oil ◽  
Vegetable Oils ◽  
Acid Methyl Ester ◽  
Waste Cooking Oil ◽  
Pyrolysis Gas ◽  
Fa Composition ◽  
Acid Methyl ◽  
Waste Cooking Oils ◽  
Cooking Oils

Abstract Vegetable oils have been used as a feedstock for fatty acid methyl ester (FAME) production. The high cost of neat vegetable oil and its impact on food security have necessitated its replacement as a feedstock for FAME by used vegetable oil, also known as waste cooking oil (WCO). This study compares the properties and fatty acid (FA) compositions of samples of neat vegetable oil with those of samples of WCO, collected from restaurants and takeaway outlets at the point of disposal. The samples were subjected to property determination and pyrolysis gas chromatography mass spectrometer (PYGCMS) analysis. Analysis showed that degree of usage and the type of food items originally fried in the oil substantially affected its properties and FA composition. Density of neat vegetable oil varied between 904.3 and 919.7 kg/m3 and of WCO between 904.3 and 923.2 kg/m3. The pH of neat vegetable oil varied between 7.38 and 8.63 and of WCO between 5.13 and 6.61. The PYGCMS analysis showed that neat palm oil contains 87.7% unsaturated FA and 12.3% saturated FA, whereas neat sunfoil contains 74.37% saturated FA and 25% polyunsaturated FA. Generally, neat vegetable oils consisted mainly of saturated FAs and polyunsaturated FAs, whereas the WCO contained mainly of saturated FAs and monounsaturated FAs. This research confirms the suitability of WCO as feedstock for FAME.

Intensification of waste cooking oil transformation by transesterification and esterification reactions in oscillatory baffled and microstructured reactors for biodiesel production

2014 ◽  
Vol 3 (6) ◽  
Author(s):  
Alex Mazubert ◽  
Joelle Aubin ◽  
Sébastien Elgue ◽  
Martine Poux
Keyword(s):  
Fatty Acid ◽  
Acid Methyl Ester ◽  
Waste Cooking Oil ◽  
Biodiesel Production ◽  
Cooking Oil ◽  
Acid Methyl ◽  
Waste Cooking Oils ◽  
Microstructured Reactors ◽  
Esterification Reactions ◽  
Cooking Oils

AbstractThe transformation of waste cooking oils for fatty acid methyl ester production is investigated in two intensified technologies: microstructured Corning

Transesterifcation of Palm Olein Oil Using Na3PO4 as Heterogeneous Catalyst

2013 ◽  
Vol 724-725 ◽  
pp. 1181-1186
Author(s):  
Khritsayaporn Thinnakorn ◽  
Jirdsak Tscheikuna
Keyword(s):  
Heterogeneous Catalyst ◽  
Palm Olein ◽  
Operating Temperature ◽  
Acid Methyl Ester ◽  
Transesterification Reaction ◽  
Molar Ratio ◽  
Order Kinetic ◽  
Rate Of Reaction ◽  
Order Kinetic Model ◽  
Olein Oil

Fatty acid methyl ester (FAME) production from transesterification reaction of palm olein oil with methanol in the presence of Na3PO4as heterogeneous catalyst was investigated. The effects of molar ratio of methanol to oil, amount of catalyst and reaction temperature on the yield of FAME were studied. The results showed that sodium phosphate can be used effectively as heterogeneous catalyst in transesterification reaction. The rate of reaction and yield of FAME depend on molar ratio of methanol to oil, amount of catalyst used and operating temperature. Molar ratio of methanol to oil of higher than 18:1 gives fastest rate of reaction and highest FAME content. Higher operating temperatures tend to accelerate the rate of reaction but reduces glycerol by-product quality. When large excess of methanol is used, the experimental results agrees with irreversible 1storder kinetic model and the activation energy is found to be 43.6 kJ/mol.

scholarly journals Ethanolysis of Waste Cooking oils using KOH Catalyst

2021 ◽  
Vol 37 (6) ◽  
pp. 1344-1349
Author(s):  
Aboulbaba Eladeb ◽  
Abdelkarim Aydi ◽  
Ibrahim Alenezi
Keyword(s):  
Gas Chromatography ◽  
Reaction Time ◽  
Potassium Hydroxide ◽  
Catalyst Concentration ◽  
Maximum Yield ◽  
Ethyl Esters ◽  
Molar Ratio ◽  
Stirring Rate ◽  
Waste Cooking Oils ◽  
Cooking Oils

The transesterification of waste cooking oils (WCO) with ethanol was investigated by means of potassium hydroxide (KOH) as catalyst. This work aimed to study the influences of catalyst concentration, temperature, ethanol to WCO molar ratio, reaction time, and stirring rate on the biodiesel conversion. Gas chromatography (GC) was used during the process of transesterification to determine the evolution of ethyl esters concentration with time. Biodiesel with maximum yield was obtained (92.5%) when 2 wt% KOH, temperature of 75°C, and ethanol/oil molar ratio of 11:1 were utilized.

scholarly journals Modeling and Optimization of Microwave-Based Bio-Jet Fuel from Coconut Oil: Investigation of Response Surface Methodology (RSM) and Artificial Neural Network Methodology (ANN)

Energies ◽  
2021 ◽  
Vol 14 (2) ◽  
pp. 295
Author(s):  
Mei Yin Ong ◽  
Saifuddin Nomanbhay ◽  
Fitranto Kusumo ◽  
Raja Mohamad Hafriz Raja Shahruzzaman ◽  
Abd Halim Shamsuddin
Keyword(s):  
Statistical Tests ◽  
Coconut Oil ◽  
Jet Fuel ◽  
Molar Ratio ◽  
Ann Model ◽  
Fuel Production ◽  
Turbine Engine ◽  
Renewable Fuel ◽  
American Society ◽  
Better Than

In this study, coconut oils have been transesterified with ethanol using microwave technology. The product obtained (biodiesel and FAEE) was then fractional distillated under vacuum to collect bio-kerosene or bio-jet fuel, which is a renewable fuel to operate a gas turbine engine. This process was modeled using RSM and ANN for optimization purposes. The developed models were proved to be reliable and accurate through different statistical tests and the results showed that ANN modeling was better than RSM. Based on the study, the optimum bio-jet fuel production yield of 74.45 wt% could be achieved with an ethanol–oil molar ratio of 9.25:1 under microwave irradiation with a power of 163.69 W for 12.66 min. This predicted value was obtained from the ANN model that has been optimized with ACO. Besides that, the sensitivity analysis indicated that microwave power offers a dominant impact on the results, followed by the reaction time and lastly ethanol–oil molar ratio. The properties of the bio-jet fuel obtained in this work was also measured and compared with American Society for Testing and Materials (ASTM) D1655 standard.

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