scholarly journals Production of Biodiesel by Transesterification Reaction of Waste Cooking Oil

2020 ◽  
pp. 1-12
Author(s):  
Donald Raoul Tchuifon Tchuifon ◽  
Serges Bruno Lemoupi Ngomade ◽  
George Nche Ndifor-Angwafor ◽  
Paul Alain Nanssou Kouteu ◽  
Tchoumboue Nsah-Ko ◽  
...  
Keyword(s):  
Physicochemical Characterization ◽  
Calorific Value ◽  
Physicochemical Characteristics ◽  
Waste Cooking Oil ◽  
Acid Number ◽  
Transesterification Reaction ◽  
Molar Ratio ◽  
Homogeneous Catalyst ◽  
Cooking Oil ◽  
Living Organisms

Waste cooking oils are an agro-food waste with adverse effects on the health of living organisms and the environment. The main objective of this work is to valorize waste cooking oil for the synthesis and physicochemical characterization of biodiesel. The method used is based on the transesterification reaction of the oils using methanol and a basic homogeneous catalyst. In this study we employ waste from refined palm oil used for frying doughnuts. After optimization a reaction time of 2 hours, KOH catalyst, and a molar ratio of 9:1 were selected to obtain a good quality biodiesel. Physicochemical characterization was performed on the biodiesel to obtain its density, viscosity, calorific value, acid number, saponification index and IR spectral features. The analysis shows that the biodiesel obtained after transesterification has physicochemical characteristics similar to those of diesel and is consistent with American standards.

scholarly journals Waste cooking oil processing for fatty acid methyl ester and mono glycerides production with magnetite catalyst

Food Research ◽  
2020 ◽  
Vol 4 (S1) ◽  
pp. 220-226
Author(s):  
Widayat ◽  
Hadiyanto ◽  
D.A. Putra ◽  
Nursafitri I. ◽  
H. Satriadi ◽  
...  
Keyword(s):  
Acid Methyl Ester ◽  
Chemical Precipitation ◽  
Waste Cooking Oil ◽  
Acid Number ◽  
Biodiesel Production ◽  
National Standard ◽  
Molar Ratio ◽  
Oil Processing ◽  
Cooking Oil ◽  
Acid Methyl

The objective of this research was to produce biodiesel using waste cooking oil and various magnetite catalysts with the esterification-transesterification process. Magnetite catalysts tested were α- Fe2O3, α- Fe2O3/Al2O3, α- Fe2O3/ZSM-5 catalysts. Catalysts were prepared through chemical precipitation and calcination. The esterificationtransesterification process was carried out with the conditions WCO: methanol molar ratio of 15:1, catalyst (1% wt of oil), heated at 65℃ for 3 hrs. The results showed biodiesel production using α- Fe2O3-ZSM-5 catalyst obtained higher %FAME (83.28%), yield (91.915%) and monoglyceride content (16.72%) compared to others due to larger pore volume. Biodiesel produced passed the requirement of Indonesian National Standard (SNI) based on density, acid number and viscosity.

scholarly journals UTILIZATION BAYAH BANTEN ZEOLITE AS A CATALYST AND BACTERIA AS A PRETREATMENT FOR BIODIESEL FROM WASTE COOKING OIL

2018 ◽  
Vol 2 (2) ◽  
pp. 85-92
Author(s):  
F. Fitriyah ◽  
Frebhika Sri Puji Pangesti
Keyword(s):  
Natural Zeolite ◽  
Phosphorus Content ◽  
Zeolite Catalyst ◽  
Waste Cooking Oil ◽  
Acid Number ◽  
Biodiesel Production ◽  
Homogeneous Catalyst ◽  
Cooking Oil ◽  
Rhizopus Sp ◽  
Research Show

ABSTRAK Pemanfaatan zeolit alam Bayah Banten sebagai katalis homogen dalam penelitian ini adalah sebagai alternatif penggunaan katalis sintetik. Selain itu bakteri Rhizopus sp. digunakan sebagai pretreatment biokatalis dalam pemanfaatan minyak jelantah untuk pembuatan biodiesel. Hal ini akan memberikan beberapa keuntungan, yaitu dapat mereduksi limbah minyak jelantah,  mengurangi biaya produksi pembuatan bahan bakar serta memanfaatkan kekayaan alam terutama yang terdapat di Provinsi Banten. Penelitian ini bertujuan mempelajari metode pembuatan biodiesel dari minyak jelantah menggunakan katalis zeolit alam Bayah dan biokatalis bakteri  Rhizopus sp serta uji kualitatif dan kuantitatif standar biodiesel. Metode yang digunakan dalam penelitian ini adalah reaksi esterifikasi/transesterifikasi minyak dengan alkohol rantai pendek melalui bantuan katalis. Hasil penelitian ini menunjukan minyak jelantah yang sudah diolah menjadi  biodiesel, yaitu viskositas (pada suhu  40°C) sebesar 0,862 g/ml dan 29,7, kadar air 0,05 % , titiknyala 120°C, titiktuang 18°C, bilangan asam 0,49 mg KOH/g, angka setana 55, belerang 0,11 mg/kg, fosfor 1,7 mg/kg, waktu bakar 43 detik, residu 1,8 % , sisa pembakaran 9,6% telah memenuhi standar biodiesel SNI-04-7182-201 Kata Kunci : biodiesel, zeolite bayah, minyak jelantah   ABSTRACT Utilization of Banten Bayah natural zeolite as a homogeneous catalyst in making biodiesel is an alternative to the use of synthetic catalysts. In addition, the bacteria Rhizopus sp., was used as a biocatalyst in waste cooking oil for the manufacture of biodiesel. This will provide several advantages, reduces waste cooking oil, reduce cost biodiesel production and utilize natural resources, especially those found in Banten Province. This study aims to study the method of making biodiesel from waste cooking oil using natural Bayah zeolite catalyst and Rhizopus sp bacterial as biocatalyst as the quantitative and quantitative standard tests of biodiesel. The methods in this study is the esterification / transesterification reaction of oil with short chain alcohols through of a catalyst. The results of this research show that waste cooking oil has been processed into biodiesel that is density and viscosity parameters (at 40°C ) is 0.862 g/mL and 29.7, 0.05% moisture content 120 ° C point, 18 ° C point, acid number is 0.49 mg KOH / g, setana number 55, sulfur content 0.11 mg / kg, phosphorus content 1.7 mg / kg, burn time 43 seconds, residue 1.8%, residual combustion 9.6% it has fulfilled the biodiesel standard SNI-04-7182-2012. Keyword : biodiesel, zeolite bayah, bacteria, cooking oil

scholarly journals The Effect of CaO Catalyst Mass from Golden Snail Shell (Pomacea Canaliculata Lamarck) on Transesterification Reaction

2021 ◽  
Vol 4 (2) ◽  
pp. 88-92
Author(s):  
Fachtur Rahman ◽  
Siti Rodiah
Keyword(s):  
Alternative Energy ◽  
Waste Cooking Oil ◽  
Transesterification Reaction ◽  
Molar Ratio ◽  
Pomacea Canaliculata ◽  
Optimum Amount ◽  
Environment Friendly ◽  
Snail Shell ◽  
Cooking Oil ◽  
Gas Chromatography Mass Spectroscopy

Biodiesel derived from waste encourages the development of environment-friendly alternative energy. One of the wastes that can be used as biodiesel is waste cooking oil. Biodiesel from waste cooking oil has some advantages such as non-toxic, less Carbon monoxide (CO), and environment-friendly. The produce of biodiesel from waste cooking oil was through transesterification reaction using CaO catalyst derived from golden snail shell. This study aimed to determine the optimum amount of catalyst that produced the highest yield. In this study, methanol was used as solvent by the molar ratio of methanol/waste cooking oil of 30:1, reaction temperature of 65˚C, reaction time for 2 hour, and variations of amount catalyst 3%, 5% and 7% by weight waste cooking oil. Biodiesel was analyzed by Gas Chromatography-Mass Spectroscopy showed that the highest yield achieved using 7% catalyst amounts was 93.28%.

scholarly journals CHARACTERISTICS OF BIODIESEL FROM WASTE COOKING OIL USING PALM EMPTY ASH CATALYST

2016 ◽  
Vol 3 (1) ◽  
pp. 38-47
Author(s):  
Sukma Budi Ariyani ◽  
Asmawit ◽  
Hidayati
Keyword(s):  
Reaction Time ◽  
Cetane Number ◽  
Calorific Value ◽  
Waste Cooking Oil ◽  
Acid Number ◽  
Phosphorus Acid ◽  
Independent Variables ◽  
Empty Fruit Bunches ◽  
Cooking Oil ◽  
Used Cooking Oil

The purpose of this study was to know the effect of adding a catalyst ash of palm empty fruit bunches on the number and characteristics of biodiesel produced from used cooking oil. The independent variables studied are heavy ash of palm empty fruit bunches (8, 10 and 12 g), the mole ratio of methanol: oil (6: 1, 9: 1 and 12: 1) and reaction time (60, 90 and 120 minutes). The results obtained are highest biodiesel yield is obtained of 54.7 mg/Kg on a reaction time of 60 minutes, the mole ratio of methanol:oil at 12:1, catalyst ash 10 g per 75 mL of methanol at a temperature of 60oC and stirring speed 600 rpm. Characteristics of biodiesel were analyzed in the study include the density, kinematic viscosity, cetane number, flash point, the point of fog, carbon residue, distillation temperature 90% vol, phosphorus, acid number and calorific value.

Application of Calcium Methoxide as Solid Base Catalyst for Biodiesel Production from Waste Cooking Oil

2016 ◽  
Vol 723 ◽  
pp. 594-598 ◽  
Author(s):  
Nichaonn Chumuang ◽  
Vittaya Punsuvon
Keyword(s):  
Reaction Temperature ◽  
Catalyst Concentration ◽  
Waste Cooking Oil ◽  
Transesterification Reaction ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Solid Base ◽  
Base Catalyst ◽  
Solid Base Catalyst ◽  
Cooking Oil

In this study, the biodiesel production of waste cooking oil using calcium methoxide as solid base catalyst was investigated. The calcium methoxide catalyst was synthesized from calcined quick lime reacted with methanol. The XRD result showed that the catalyst was successfully synthesized with sufficient purity. The strength of catalyst was examined on the transesterification reaction of waste cooking oil and methanol. Parameters affecting on transesterification such as the catalyst concentration, methanol-to-oil-molar ratio, reaction time and reaction temperature were investigated. The results showed that the percentage of fatty acid methyl ester conversion of 99.06%. The optimum conditions were achieved within 3 h using 3wt% catalyst concentration, 12:1 methanol-to-oil molar ratio and 65°C reaction temperature. In addition, the kinetic study of transesterification reaction was carried out at the temperature from 30°C to 65°C. The pseudo-first order was good agreement with the experiment results. The reaction rate constant (k) and activated energy (Ea) were determined as 0.023 min-1 and 55.77 kJ/mol, respectively.

scholarly journals TRANSESTERIFICATION OF BIODIESEL FROM WASTE COOKING OIL USING CAO NANOCATALYST

Konversi ◽  
2019 ◽  
Vol 8 (2) ◽  
Author(s):  
Cindi Ramayanti ◽  
Sarah Dampang
Keyword(s):  
Raw Materials ◽  
Waste Cooking Oil ◽  
Acid Number ◽  
Production Costs ◽  
Raw Material ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Second Stage ◽  
Cooking Oil ◽  
Initial Stage

The production costs of biodiesel based on vegetable oil is not economical, so it is difficult for biodiesel to compete with petrodiesel. Waste cooking oil can be used as a source of raw materials for biodiesel production. This research aims to produce biodiesel from waste cooking oil. The initial stage is to pretreatment of waste cooking oil. At this step, the waste cooking oil is filtered to separate impurities from the raw material. After that, it is heated to 100 oC to remove the water content. The second stage is transesterification. At this stage, the reaction time remains for one hour at a temperature of 65 oC. the product is centrifuged to separate the catalyst. The highest yield was obtained in the 12: 1 molar ratio variable and the amount of catalyst 3%, which was 0.922. Yield obtained ranged from 0.853-0.922. An increase in the molar ratio is significant enough to increase the amount of yield. However, increasing the amount of catalyst especially from 2% to 3% is not significant enough to increase biodiesel yield. The characteristics of biodiesel produced are in accordance with SNI Biodiesel, density 870 Kg / cm3, viscosity 4.25 cSt, flash point 170, and acid number 0.4 mg-KOH/g biodiesel.

scholarly journals Production of Biodiesel Fuel from Waste Soya bean Cooking Oil by Alkali Trans-esterification Process

2016 ◽  
Vol 11 (1) ◽  
pp. 260-266
Author(s):  
Ajinkya Deshpande ◽  
Pratiksinh Chavda ◽  
Heena Kadeval
Keyword(s):  
Relative Density ◽  
Volume Ratio ◽  
Calorific Value ◽  
Acid Value ◽  
Waste Cooking Oil ◽  
Single Step ◽  
Soya Bean ◽  
Biodiesel Fuel ◽  
Homogeneous Catalyst ◽  
Cooking Oil

Biodiesel is biodegradable, clean-burning, non-toxic, renewable, high-quality, and cheap diesel fuel made primarily from waste vegetable oil which can be used without any alterations in engine design. The paper is concerned with the extraction and quality evaluation of the biodiesel fuels synthesized from waste soya bean cooking oil. Waste soya bean cooking oil had high amount of free fatty acid. Thus, single step transesterification process with the aid of homogeneous catalyst as 1% potassium hydroxide were implemented in this experiment. Methanol was chosen as alcohol solvent. In the transesterification process, the triglycerides in waste cooking oil was reacted with a methanol to form esters and glycerol as by product.The biodiesel were extracted for different oil to methanol ratio as 1:2, 1:3 and 1:4. The highest biodiesel yield of 76% was obtained at 1:3 volumetric ratio for 60 ºC reaction temperature and 1250 rpm stirring speed. Results show that the optimal methyl ester yield of 90% occurred at methanol: oil volume ratio of 3:1. The product met the ASTM fuel standards for relative density, acid value, relative density, calorific value, flash point and kinematic viscosity.

scholarly journals Biodiesel Synthesis From Waste Cooking Oil Using CaO.SrO Catalyst By Transesterification Reaction In Batch Reactor

2018 ◽  
Vol 7 (2) ◽  
pp. 136-141
Author(s):  
Nuni Widiarti ◽  
Ismi Arinal Haq ◽  
F. Widhi Mahatmanti ◽  
Harjito Harjito ◽  
Cepi Kurniawan ◽  
...  
Keyword(s):  
Catalytic Activity ◽  
Surface Area ◽  
Catalyst Surface ◽  
Batch Reactor ◽  
Waste Cooking Oil ◽  
Transesterification Reaction ◽  
Molar Ratio ◽  
Cooking Oil ◽  
Biodiesel Synthesis ◽  
And Shifts

CaO is a very good catalyst for oil transesterification reactions into biodiesel, but requires a reaction time of 2 hours to obtain equilibrium. The time of CaO catalysis reaction can be accelerated by modifying the CaO catalyst with SrO. Synthesis biodiesel of waste cooking oil has been successfully conducted by transesterification reaction that used batch reactor assisted by CaO.SrO catalyst. The aim of this study is to determine the characteristics and catalytic activity of catalyst in the transesterification reaction. Catalysts have been successfully synthesized by coprecipitation method with oil to methanol molar ratio of 1:1, and its calcined at 800oC for 3 hours. Catalyst was characterized by XRD to determine the crystallinity. The smaller catalyst crystallinity obtained as the decline in intensity and shifts diffraction angles of CaO modified SrO catalyst. Surface area of catalyst characterized by SAA, that allow surface area between CaO modified SrO by 10.217 m2/g. Transesterification reaction performed on variation time (30, 60, 90, 120, 150 minutes), and the catalysts amount (1, 2, 4, 6, 8% w/v). The optimum condition of catalytic activity in reaction for 2 hours and the catalyst amount is 1% w/v of reactants that produce yield of biodiesel is 96.4%.

Identification of Methyl Ester Content from Waste Cooking Oil Using Gas Chromatographic Method

2014 ◽  
Vol 660 ◽  
pp. 297-300
Author(s):  
Nor Hazwani Abdullah ◽  
Sulaiman Hassan
Keyword(s):  
Gas Chromatography ◽  
Methyl Ester ◽  
Acid Methyl Ester ◽  
Waste Cooking Oil ◽  
Molar Ratio ◽  
Ionization Detector ◽  
Cooking Oil ◽  
Ester Content ◽  
Flame Ionization ◽  
Acid Methyl

Waste cooking oil has always been an environment problem in food factories and one method of effect disposing this oil without effecting the environment is to convert it to fatty acid methyl ester (FAME) using small scale pilot plant. The conversion of waste cooking oil with sodium hydroxide as a catalyst in conversional process at 22kHz speed. The reaction of time, molar ratio, speed, catalyst and amount of catalyst will be effect in FAME quality. The quality of biodiesel define is total ester content using gas chromatography. Gas chromatography analysis is a one of technique for identification and quantitation of compounds in a biodiesel sample. From biodiesel sample can identification of contaminants and fatty acid methyl ester. In this research biodiesel sample were analyses using a gas chromatography-flame ionization detector ( Perkin Elmer GC Model Clarus 500) equipped with a DB-5 HT capillary column ( 0.53mm x 5 m) J&W Scientific. The analytic conditions for ester content were as follow by: column temperature used 2100C, temperature flame ionization detector (FID) of 2500C, pressure of 80kPa, flow carrier gas of 1ml/min, temperature injector of 2500C, split flow rate of 50ml/min, time for analysis 20 minute and volume injected of 1 μl. The ester content (C), expresses as a mass fraction in present using formula (EN 14103, 2003a) calculation. Conversion of triglyceride (TG) to FAME using conversional process obtained 96.54 % w.t with methanol to oil molar ratio 6:1, 1%w.t acid sulphuric and 1% w.t sodium hydroxide catalyst.

Production of Biodiesel from Waste Cooking Oil via Ultrasonic-Assisted Catalytic System

2014 ◽  
Vol 699 ◽  
pp. 552-557 ◽  
Author(s):  
Norzita Ngadi ◽  
Lai Nyuk Ma ◽  
Hajar Alias ◽  
Anwar Johari ◽  
Roshanida Abd Rahman ◽  
...  
Keyword(s):  
Calcium Oxide ◽  
Catalyst Concentration ◽  
Waste Cooking Oil ◽  
Molar Ratio ◽  
Catalyst Amount ◽  
Cooking Oil ◽  
Used Oil ◽  
Ultrasonic Assisted ◽  
Transesterification Method ◽  
Percentage Conversion

In this study, production of biodiesel from waste cooking oil (WCO) was carried out via ultrasonic-assisted transesterification method. Calcium oxide (CaO) was used as a catalyst. The effects of methanol to oil molar ratio, reaction temperature and the catalyst amount towards the percentage conversion of oil to biodiesel were investigated. The biodiesel produced was analyzed using GC-FID method. The results obtained showed that 82 % of oil was successfully converted into biodiesel. This indicates that the used oil (WCO) has the potential to be the future source of biodiesel. Catalyst concentration of 3 w/w%, methanol to oil molar ratio of 15:1 and temperature of 65°C are the best condition for the conversion of oil to biodiesel. The result obtained was found out that, methanol to oil molar ratio and catalyst amount has given significant effect on the conversion of oil. However, temperature ranged from (35 to 75) °C apparently, showed no significant effect on percentage conversion of oil.

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