scholarly journals PRODUKSI BIODIESEL DARI LEMAK SAPI DENGAN PROSES TRANSESTERIFIKASI DENGAN KATALIS BASA NaOH

2013 ◽  
Vol 2 (1) ◽  
pp. 1-6
Author(s):  
Ranggita Dwi Nindya Affandi ◽  
Toni Rizki Aruan ◽  
Taslim ◽  
Iriany
Keyword(s):  
Reaction Time ◽  
Beef Tallow ◽  
Low Cost ◽  
Maximum Yield ◽  
Single Step ◽  
Raw Material ◽  
Biodiesel Production ◽  
National Standard ◽  
Molar Ratio ◽  
Reflux Condenser

Biodiesel is an alternative fuel commonly produced from vegetable oil or animal fat with methanol through transesterification. Beef tallow was used as a raw material of transesterification to make biodiesel, because the price of beef tallow was driven down by the market and to reduce the pollution to the surrounding. In this research variable observed were reaction temperature, reaction time and amount of catalyst. Transesterification was carried out in a three necked spherical Pyrex vessel equipped with reflux condenser, stirrer and thermometer. In the present investigation an attempt has been made to use beef tallow as low cost sustainable potential feedstock for biodiesel production by single step transesterification process. Under optimal condition, the maximum yield of 95,67 % beef tallow methyl ester was obtained by using 6 : 1 molar ratio of beef tallow to methanol at 50 oC for a reaction time 30 minutes in the presence of 0,8 wt% of NaOH catalyst. The biodiesel properties were comparable to Indonesian National Standard (SNI). The results of this work showed that the use of beef tallow is suitable for feedstock of biodiesel production with low cost.

scholarly journals PENGARUH SUHU REAKSI DAN JUMLAH KATALIS PADA PEMBUATAN BIODIESEL DARI LIMBAH LEMAK SAPI DENGAN MENGGUNAKAN KATALIS HETEROGEN CaO DARI KULIT TELUR AYAM

2015 ◽  
Vol 4 (1) ◽  
pp. 35-41 ◽  
Author(s):  
Wendi ◽  
Valentinoh Cuaca ◽  
Taslim
Keyword(s):  
Methyl Ester ◽  
Beef Tallow ◽  
Low Cost ◽  
Maximum Yield ◽  
Raw Material ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Animal Fats ◽  
Acid Catalyzed ◽  
Methyl Ester Content

Biodiesel is an alternative fuel for diesel engines consisting of the alkyl monoesters from vegetable oils or animal fats. Beef tallow waste is the non-edible raw material with low cost production and the availability is huge in the cattle production. The objective of the study was to utilize beef tallow waste for biodiesel production using solid oxide catalyst which derived from the industrial eggshells. The materials calcined with temperature 900oC and time 2 hours, transformed calcium species in the shells into active CaO catalysts.The oil contained high free fatty acid (FFA) content of 1.86%. The FFA content of the oil was reduced by acid-catalyzed esterification. The product from this stage was subjected to produce biodiesel. Transesterification process reacts oil and methanol to produce methyl ester and glycerol. The produced methyl ester on the upper layer was separated from the glycerol and then washed. Effect of various process variables such as amount of catalyst and temperature were investigated. The biodiesel properties like methyl ester content, density, viscosity, and flash point was evaluated and was found to compare well with Indonesian Standard (SNI). Under the best condition, the maximum yield of 82.43% beef tallow methyl ester was obtained by using 9:1 molar ratio of methanol to beef tallow oil at 55oC, for a reaction time 1.5 hours in the presence 3 wt% of CaO catalyst. The results of this work showed that the use of beef tallow is very suitable as low cost feedstock for biodiesel production.

Natural Hydroxyapatite (NHAp) Derived from Pork Bone as a Renewable Catalyst for Biodiesel Production via Microwave Irradiation

2015 ◽  
Vol 659 ◽  
pp. 216-220 ◽  
Author(s):  
Achanai Buasri ◽  
Thaweethong Inkaew ◽  
Laorrut Kodephun ◽  
Wipada Yenying ◽  
Vorrada Loryuenyong
Keyword(s):  
Reaction Time ◽  
Microwave Power ◽  
Raw Materials ◽  
Raw Material ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Catalyst Loading ◽  
X Ray ◽  
Animal Bone ◽  
Natural Hydroxyapatite

The use of waste materials for producing biodiesel via transesterification has been of recent interest. In this study, the pork bone was used as the raw materials for natural hydroxyapatite (NHAp) catalyst. The calcination of animal bone was conducted at 900 °C for 2 h. The raw material and the resulting heterogeneous catalyst were characterized using X-ray diffraction (XRD), X-ray fluorescence (XRF), scanning electron microscopy (SEM) and the Brunauer-Emmett-Teller (BET) method. The effects of reaction time, microwave power, methanol/oil molar ratio, catalyst loading and reusability of catalyst were systematically investigated. The optimum conditions, which yielded a conversion of oil of nearly 94%, were reaction time 5 min and microwave power 800 W. The results indicated that the NHAp catalysts derived from pork bone showed good reusability and had high potential to be used as biodiesel production catalysts under microwave-assisted transesterification of Jatropha Curcas oil with methanol.

Biodiesel Production From Crude Rubber Seed Oil Using Supercritical Methanol Transesterification

2015 ◽  
Vol 781 ◽  
pp. 655-658 ◽  
Author(s):  
Thakun Sawiwat ◽  
Somjai Kajorncheappunngam
Keyword(s):  
Reaction Time ◽  
Seed Oil ◽  
Raw Material ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Supercritical Methanol ◽  
Rubber Seed Oil ◽  
Promising Alternative ◽  
Rubber Seed ◽  
Biodiesel Synthesis

Synthesis of biodiesel from rubber seed oil using a supercritical methanol was investigated under various reaction conditions (220 - 300°C, 80 - 180 bar) with reaction time of 1-15 min and oil:methanol molar ratio of 1:20 - 1:60. Free fatty acid methyl esters (FAMEs) content were analyzed by gas chromatography-mass spectroscopy (GC-MS). Most properties of produced biodiesel were in good agreement with biodiesel standard (EN 14214). The maximum FAME yield of 86.90% was obtained at 260°C, 160 bar, 5 min reaction time using oil:methanol molar ratio of 1:40. The result showed the acid value of rubber seed oil decreased to 0.58 mgKOH/g from initial 24 mgKOH/g to. It could be concluded from this findings that crude rubber seed oil is a promising alternative raw material for biodiesel synthesis via supercritical methanol tranesterification.

Current scenario of catalysts for biodiesel production: a critical review

2018 ◽  
Vol 34 (2) ◽  
pp. 267-297 ◽  
Author(s):  
Farrukh Jamil ◽  
Lamya Al-Haj ◽  
Ala’a H. Al-Muhtaseb ◽  
Mohab A. Al-Hinai ◽  
Mahad Baawain ◽  
...  
Keyword(s):  
Heterogeneous Catalysts ◽  
Low Cost ◽  
Bifunctional Catalyst ◽  
Raw Material ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Homogeneous Catalysts ◽  
Animal Fats ◽  
Current Scenario ◽  
Short Chain Alcohol

AbstractDue to increasing concerns about global warming and dwindling oil supplies, the world’s attention is turning to green processes that use sustainable and environmentally friendly feedstock to produce renewable energy such as biofuels. Among them, biodiesel, which is made from nontoxic, biodegradable, renewable sources such as refined and used vegetable oils and animal fats, is a renewable substitute fuel for petroleum diesel fuel. Biodiesel is produced by transesterification in which oil or fat is reacted with short chain alcohol in the presence of a catalyst. The process of transesterification is affected by the mode of reaction, molar ratio of alcohol to oil, type of alcohol, nature and amount of catalysts, reaction time, and temperature. Various studies have been carried out using different oils as the raw material; different alcohols (methanol, ethanol, butanol); different catalysts; notably homogeneous catalysts such as sodium hydroxide, potassium hydroxide, sulfuric acid, and supercritical fluids; or, in some cases, enzymes such as lipases. This article focuses on the application of heterogeneous catalysts for biodiesel production because of their environmental and economic advantages. This review contains a detailed discussion on the advantages and feasibility of catalysts for biodiesel production, which are both environmentally and economically viable as compared to conventional homogeneous catalysts. The classification of catalysts into different categories based on a catalyst’s activity, feasibility, and lifetime is also briefly discussed. Furthermore, recommendations have been made for the most suitable catalyst (bifunctional catalyst) for low-cost oils to valuable biodiesel and the challenges faced by the biodiesel industry with some possible solutions.

Optimization of Esterification and Transesterification Reactions for Biodiesel Production from Crude Coconut Oil Using RSM Techniques

2016 ◽  
Vol 723 ◽  
pp. 610-615 ◽  
Author(s):  
Natta Pimngern ◽  
Vittaya Punsuvon
Keyword(s):  
Fatty Acid ◽  
Reaction Time ◽  
Acid Methyl Ester ◽  
Coconut Oil ◽  
Raw Material ◽  
Biodiesel Production ◽  
Quadratic Model ◽  
Molar Ratio ◽  
Optimum Conditions ◽  
Model Equations

Crude coconut oil with high free fatty acid (FFA) content was used as a raw material to produce biodiesel. In this work, the esterification followed by transesterification of crude coconut oil with methanol is studied. The response surface methodology (RSM) with 5-level-3-factor central composite design (CCD) was applied to study the effect of different factors on the FFA content of esterification and the percentage of fatty acid methyl ester (FAME) conversion of transesterification. The FAME conversion was detected by proton magnetic resonance (1H-NMR) spectrometer. As a result, the optimum conditions for esterification were 6:1 of methanol-to-oil molar ratio, 0.75wt% of sulfuric acid (H2SO4) concentration and 90 min of reaction time. The optimum conditions for transesterification were 8.23:1 of methanol-to-oil molar ratio, 0.75wt% of sodium hydroxide (NaOH) concentration and 80 min of reaction time. Quadratic model equations were obtained describing the relationships between dependents and independent variables to minimize the FFA content and maximize the FAME conversion. Fuel properties of the crude coconut oil biodiesel were also examined followed ASTM and EN standards. The results showed that all properties met well with both standards.

Hybrid Approach for Optimizing Process Parameters in Biodiesel Production from Palm Oil

2020 ◽  
Vol 834 ◽  
pp. 16-23
Author(s):  
Pongchanun Luangpaiboon ◽  
Pasura Aungkulanon
Keyword(s):  
Reaction Time ◽  
Process Parameters ◽  
Reaction Temperature ◽  
Palm Oil ◽  
Hybrid Approach ◽  
Maximum Yield ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Optimization Approach ◽  
Influential Parameters

Biodiesel was synthesized from direct transesterification of palm oil reacted with methanol in the presence of a suitable catalyst. There is a sequence of three consecutive reversible reactions for the transesterification process. These process parameters were optimized via the hybrid optimization approach of a conventional response surface method and artificial intelligence mechanisms from Sine Cosine and Thermal Exchange Optimization metaheuristics. The influential parameters and their combined interaction effects on the transesterification efficiency were established through a factorial designed experiments. In this study, the influential parameters being optimized to obtain the maximum yield of biodiesel were reaction temperature of 60–150°C, reaction time of 1–6 hours, methanol to oil molar ratio of 6:1–12:1 mol/mol and weight of catalyst of 1–10wt. %. On the first phase, the analysis of variance (ANOVA) revealed the reaction time as the most influential parameter on biodiesel production. Based on the experimental results from the hybrid algorithm via the SCO, it was concluded that the optimal biodiesel yield for the transesterification of palm oil were found to be 100°C for reaction temperature, 4 hours for reaction time, 10:1 wt/wt of ratio methanol to oil and 8% of weight of catalyst with 92.15% and 90.97% of biodiesel yield for expected and experimental values, respectively.

Two-Step Preparation of Bio-Diesel from the Used Bleaching Clay

2012 ◽  
Vol 209-211 ◽  
pp. 1774-1777
Author(s):  
Su Xi Wu ◽  
Shuai Hang Yan ◽  
Hui Cai
Keyword(s):  
Reaction Time ◽  
Maximum Yield ◽  
Acid Value ◽  
Raw Material ◽  
Bleaching Clay ◽  
Molar Ratio ◽  
Alkaline Catalyst ◽  
Orthogonal Experiments ◽  
Optimal Reaction Condition ◽  
Optimal Reaction

with the shortage of the raw material oil for producing bio-diesel in China, the oil, recovered from the used bleaching clay which often be discarded by vegetable oil factory, was used to prepare bio-diesel in this trial. Two-step catalyzed process was adopted to produce biodiesel from the oil. The effect of methanol-to-oil molar ratio, alkaline catalyst quantity, reaction temperature and reaction time on the preesterification and transesterification reaction was investigated through orthogonal experiments. Thus the optimal reaction condition came out. Firstly, the optimal pre-esterification condition, under which the end acid value of the product was minimum (i.e. 1.88 mgKOH/g),was to react for 40 h at 60°C,with a methanol-to-oil molar ratio of 12:1, and by adding alkali catalyst 4% based on the oil weight. Secondly，the optimal transesterification condition, under which the maximum yield of bio-diesel can reach up to 98.2%, was to react for 2.5 h at 60°C,with the methanol-to-oil molar ratio of 7:1, and by adding catalyst 1.25% based on the oil weight.

scholarly journals OPTIMIZING REACTION CONDITIONS OF BIODIESEL PRODUCTION FROM WASTE COOKING OIL USING GREEN SOLID CATALYST

2020 ◽  
Vol 7 (8) ◽  
pp. 65-71
Author(s):  
I Nengah Simpen ◽  
I Made Sutha Negara ◽  
Sofyan Dwi Jayanto
Keyword(s):  
Reaction Time ◽  
Research Result ◽  
Waste Cooking Oil ◽  
Biodiesel Production ◽  
National Standard ◽  
Molar Ratio ◽  
Solid Catalyst ◽  
Reaction Conditions ◽  
Cooking Oil ◽  
One Step

Biodiesel production from waste cooking oil in two steps reaction of esterification and transesterification is low efficient, due to twice methanol consumption and need more reaction time. Optimizing reaction conditions of CaO as a matrix of solid catalyst prepared from crab shell (green CaO) and modified by K2O/TiO2 for converting waste cooking oil to biodiesel have been carried out. Catalytic process of waste cooking oil to biodiesel took place in one step reaction of esterification and transesterification. The research result showed that optimum conditions in its one step reaction such as methanol to oil molar ratio was 9:1, amount of CaO/K2O-TiO2 catalyst to oil was 5% and reaction time of 60 minutes with biodiesel yield was 88.24%. Physical and chemical properties of biodiesel which produced from one step reaction of esterification and transesterification of waste cooking oil were suitable with Indonesian National Standard (SNI-04-7182-2006) namely density at 40oC of 850 kg/m3, kinematic viscosity at 40oC of 3.32 cSt, water content of 0.046%, iodine number of 59.25 g I2/100g and acid value of 0.29 mg KOH/g. Gas chromatography-mass spectrometry (GC-MS) analysis of biodiesel formed fatty acid methyl esters from conversion of waste cooking oil.

scholarly journals Optimization of the Production of Enzymatic Biodiesel from Residual Babassu Oil (Orbignya sp.) via RSM

Catalysts ◽  
2020 ◽  
Vol 10 (4) ◽  
pp. 414 ◽  
Author(s):  
Katerine S. Moreira ◽  
Lourembergue S. Moura Júnior ◽  
Rodolpho R. C. Monteiro ◽  
André L. B. de Oliveira ◽  
Camila P. Valle ◽  
...  
Keyword(s):  
Low Cost ◽  
Ethyl Esters ◽  
Raw Material ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Enzymatic Esterification ◽  
Maximum Loss ◽  
Babassu Oil ◽  
Small Change ◽  
Optimized Conditions

Residual oil from babassu (Orbignya sp.), a low-cost raw material, was used in the enzymatic esterification for biodiesel production, using lipase B from Candida antarctica (Novozym® 435) and ethanol. For the first time in the literature, residual babassu oil and Novozym® 435 are being investigated to obtain biodiesel. In this communication, response surface methodology (RSM) and a central composite design (CCD) were used to optimize the esterification and study the effects of four factors (molar ratio (1:1–1:16, free fatty acids (FFAs) /alcohol), temperature (30–50 °C), biocatalyst content (0.05–0.15 g) and reaction time (2–6 h)) in the conversion into fatty acid ethyl esters. Under optimized conditions (1:18 molar ratio (FFAs/alcohol), 0.14 g of Novozym® 435, 48 °C and 4 h), the conversion into ethyl esters was 96.8%. It was found that after 10 consecutive cycles of esterification under optimal conditions, Novozym® 435 showed a maximum loss of activity of 5.8%, suggesting a very small change in the support/enzyme ratio proved by Fourier Transform Infrared (FTIR) spectroscopy and insignificant changes in the surface of Novozym® 435 proved by scanning electron microscopy (SEM) after the 10 consecutive cycles of esterification.

scholarly journals Comprehensive Comparison of Hetero-Homogeneous Catalysts for Fatty Acid Methyl Ester Production from Non-Edible Jatropha curcas Oil

Catalysts ◽  
2021 ◽  
Vol 11 (12) ◽  
pp. 1420
Author(s):  
Khawer Khan ◽  
Noaman Ul-Haq ◽  
Wajeeh Ur Rahman ◽  
Muzaffar Ali ◽  
Umer Rashid ◽  
...  
Keyword(s):  
Fatty Acid ◽  
Reaction Time ◽  
Jatropha Curcas ◽  
Low Cost ◽  
Methyl Esters ◽  
Maximum Yield ◽  
Acid Methyl Ester ◽  
Molar Ratio ◽  
Acid Methyl ◽  
Comprehensive Comparison

The synthesis of biodiesel from Jatropha curcas by transesterification is kinetically controlled. It depends on the molar ratio, reaction time, and temperature, as well as the catalyst nature and quantity. The aim of this study was to explore the transesterification of low-cost, inedible J. curcas seed oil utilizing both homogenous (potassium hydroxide; KOH) and heterogenous (calcium oxide; CaO) catalysis. In this effort, two steps were used. First, free fatty acids in J. curcas oil were reduced from 12.4 to less than 1 wt.% with sulfuric acid-catalyzed pretreatment. Transesterification subsequently converted the oil to biodiesel. The yield of fatty acid methyl esters was optimized by varying the reaction time, catalyst load, and methanol-to-oil molar ratio. A maximum yield of 96% was obtained from CaO nanoparticles at a reaction time of 5.5 h with 4 wt.% of the catalyst and an 18:1 methanol-to-oil molar ratio. The optimum conditions for KOH were a molar ratio of methanol to oil of 9:1, 5 wt.% of the catalyst, and a reaction time of 3.5 h, and this returned a yield of 92%. The fuel properties of the optimized biodiesel were within the limits specified in ASTM D6751, the American biodiesel standard. In addition, the 5% blends in petroleum diesel were within the ranges prescribed in ASTM D975, the American diesel fuel standard.

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