scholarly journals Production of methyl esters from fried soybean oil using dimethyl carbonate with hydrobromic acid

2019 ◽  
Vol 5 ◽  
pp. 1463-1469 ◽  
Author(s):  
Balaji Panchal ◽  
Shenjun Qin ◽  
Tao Chang ◽  
Yuzhuang Sun ◽  
Jinxi Wang ◽  
...  
Author(s):  
SUNNY SONI ◽  
MADHU AGARWAL

Biodiesel is a renewable liquid fuel made from natural, renewable biological sources such as edible and non edible oils. Over the last years, biodiesel has gained more market due to its benefits and because it appears as the natural substitute for diesel. Reasons for growing interest in biodiesel include its potential for reducing noxious emissions, potential contributions to rural economic development, as an additional demand center for agricultural commodities, and as a way to reduce reliance on foreign oil. Biodiesel was prepared from soybean oil by transesterification with methanol in the presence of cement clinker. Cement clinker was examined as a catalyst for a conversion of soybean oil to fatty acid methyl esters (FAMEs). It can be a promising heterogeneous catalyst for the production of biodiesel fuels from soybean oil because of high activity in the conversion and no leaching in the transesterification reaction. The reaction conditions were optimized. A study for optimizing the reaction parameters such as the reaction temperature, and reaction time, was carried out. The catalyst cement clinker composition was characterized by XRF. The results demonstrate that the cement clinker shows high catalytic performance & it was found that the yield of biodiesel can reach as high as 84.52% after 1 h reaction at 65°C, with a 6:1 molar ratio of methanol to oil, 21 wt% KOH/cement clinker as catalyst.


METANA ◽  
2019 ◽  
Vol 15 (2) ◽  
pp. 57-64
Author(s):  
Setiarto Pratigto ◽  
Istadi Istadi ◽  
Dyah Hesti Wardhani

Penelitian ini akan mengkaji kinetika reaksi transesterifikasi minyak kedelai dengan metanol menggunakan katalis CaO dengan parameter rasio mol reaktan terhadap konversi metil ester yang digunakan untuk menentukan persamaan kecepatan reaksi. Katalis CaO digunakan untuk reaksi transesterifikasi karena memiliki kekuatan basa yang tinggi, ramah lingkungan, kelarutan yang rendah dalam metanol. Kinetika reaksi untuk reaktor batch dihitung saat reaksi berlangsung berdasarkan rejim surface area limited yang menentukan. Tujuan penelitian ini untuk mengetahui bentuk persamaan kecepatan reaksi transesterifikasi minyak kedelai dan metanol menggunakan katalis CaO menurut metode differential reactor. Penelitian dilakukan dengan reaksi transesterifikasi minyak kedelai dan metanol dengan katalis CaO dengan variabel bebas perbandingan mol reaktan. Hasil penelitian mengemukakan metanol teradsorpsi di permukaan katalis dan trigliserida tidak teradsorpsi di permukaan katalis menunjukkan mekanisme reaksi katalitik Eley-Rideal. Persamaan kecepatan reaksi dapat digunakan dalam perancangan reaktor, sehingga hubungan antara konversi trigliserida menjadi biodiesel dengan kebutuhan berat katalis dan volume reaktor yang diperlukan dapat diprediksi. This study will examine the kinetics of the transesterification reaction of soybean oil with methanol using a CaO catalyst with the parameters of the mole ratio of reactants to the conversion of methyl esters used to determine the reaction velocity equation. CaO catalyst is used for transesterification reaction because it has high base strength, environmentally friendly, low solubility in methanol. The reaction kinetics for a batch reactor are calculated when the reaction takes place based on a decisive surface area limited regime. The purpose of this study was to determine the shape of the speed equation for the transesterification of soybean oil and methanol using a CaO catalyst according to the differential reactor method. The research was carried out with the transesterification reaction of soybean oil and methanol with a CaO catalyst with a free variable ratio of reactant moles. The results of the study revealed that methanol adsorbed on the surface of the catalyst and triglycerides not adsorbed on the surface of the catalyst showed an Eley-Rideal catalytic reaction mechanism. The reaction speed equation can be used in reactor design, so the relationship between the conversion of triglycerides to biodiesel with the required catalyst weight and the reactor volume required can be predicted.


1975 ◽  
Vol 55 (1) ◽  
pp. 49-59 ◽  
Author(s):  
D. W. FRIEND ◽  
J. K. G. KRAMER ◽  
F. D. SAUER ◽  
A. H. CORNER ◽  
K. M. CHARLTON ◽  
...  

One hundred and eighty weaner pigs were allotted to five dietary treatments comprising a control with no added oil and the control with either soybean oil or rapeseed oil (Brassica campestris cv. Span) each at 10 and 20% of the diet. Postmortem examinations were conducted on equal numbers of boars and gilts at the beginning of the experiment, as initial controls, and after 1, 4 and 16 wk on the experimental diets. When fed for 1 to 4 wk, the higher level of both oils reduced (P < 0.05) body weight gain but from 4 to 16 wk, differences were not significant for any of the diets. Consumption of the control diet exceeded (P < 0.05) that of any other diet, but pigs fed the oil diets showed improved (P < 0.01) feed efficiency. Minute focal interstitial infiltrations of mononuclear cells were present in the myocardium of some pigs in each dietary treatment and also in the initial controls. Foci of overt myocardial necrosis were not seen. Oil red 0 stained sections revealed traces of myocardial fat accumulation which occurred more frequently in pigs fed the high oil diets. In a second experiment, 24 weaner boar pigs were fed the control and the 10% Span oil diets. Two pigs from each treatment were killed on each of days 0, 4, 8, 12, 16 and 20. Total fat was extracted from the heart of each pig and methyl esters determined by gas–liquid chromatography. There was no significant (P = 0.05) difference in percent fat of dry matter between pigs fed the control and the 10% Span diet. The proportions of the major fatty acids were similar between diets. Erucic acid and linolenic acid were present in the cardiac lipid of all control pigs, but to a significantly (P < 0.01) lesser degree than for pigs fed the Span diet. The level of arachidonic acid, for both groups of pigs, declined (P < 0.05) progressively with the duration (days) of feeding.


RSC Advances ◽  
2018 ◽  
Vol 8 (23) ◽  
pp. 13048-13053 ◽  
Author(s):  
Wei Liu ◽  
Feifei Duan ◽  
Yanlan Bi

A sustainable method has been developed for fast transesterification of epoxidized soybean oil (ESBO) to prepare epoxy methyl esters (ESBOME) at 25 °C with NaOH as catalyst.


2011 ◽  
Vol 2011 ◽  
pp. 1-8 ◽  
Author(s):  
Elisa d'Avila Cavalcanti-Oliveira ◽  
Priscila Rufino da Silva ◽  
Alessandra Peçanha Ramos ◽  
Donato Alexandre Gomes Aranda ◽  
Denise Maria Guimarães Freire

The process of biodiesel production by the hydroesterification route that is proposed here involves a first step consisting of triacylglyceride hydrolysis catalyzed by lipase from Thermomyces lanuginosus (TL 100L) to generate free fatty acids (FFAs). This step is followed by esterification of the FFAs with alcohol, catalyzed by niobic acid in pellets or without a catalyst. The best result for the enzyme-catalyzed hydrolysis was obtained under reaction conditions of 50% (v/v) soybean oil and 2.3% (v/v) lipase (25 U/mL of reaction medium) in distilled water and at 60∘C; an 89% conversion rate to FFAs was obtained after 48 hours of reaction. For the esterification reaction, the best result was with an FFA/methanol molar ratio of 1:3, niobic acid catalyst at a concentration of 20% (w/w FFA), and 200∘C, which yielded 92% conversion of FFAs to soy methyl esters after 1 hour of reaction. This study is exceptional because both the hydrolysis and the esterification use a simple reaction medium with high substrate concentrations.


2012 ◽  
Vol 560-561 ◽  
pp. 555-562 ◽  
Author(s):  
Dan Zeng ◽  
Yang Li ◽  
Tao Fang

Biodiesel was prepared by methyl esterification and effects of different reaction conditions on the yield of fatty acid methyl esters (FAMEs) were investigated. The result of the orthogonal experiment analysis shows that the order of influential factors is ranked as reaction temperature > methanol-to-soybean-oil (M/O) ratio > reaction time. The maximum yield of 94.8 % has been achieved by reacting supercritical methanol and soybean oil in M/O ratio 4:2 (v/v) at 573 K for 45 min. Moreover, the higher M/O ratio, the higher yield of FAMEs will be obtained. At the temperature ranging from 533 k to 573 k, the yield rises significantly; however, since soybean oil decomposes over 573 K, the yield decreases oppositely. Time longer than 45 min has less effect on the final yield. In addition, the phase equilibrium data of supercritical methanol + C12 methyl esters and supercritical methanol + C18 methyl esters were separately correlated using the Peng-Robinson (PR) equation of state (EOS) with the Adachi-Sugie (AS) mixing rule.


Fuel ◽  
2016 ◽  
Vol 163 ◽  
pp. 8-16 ◽  
Author(s):  
Chachchaya Thunyaratchatanon ◽  
Apanee Luengnaruemitchai ◽  
Nuwong Chollacoop ◽  
Yuji Yoshimura

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