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Study of an ethylic biodiesel integrated process: Raw-materials, reaction optimization and purification methods

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TLDR
In this article, the authors evaluate the effectiveness of water-free purification methods for the use of a cation-exchange resin and a ceramic membrane for water free purification.
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This article is published in Fuel Processing Technology.The article was published on 2014-08-01 and is currently open access. It has received 19 citations till now. The article focuses on the topics: Waste oil & Vegetable oil.

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Citations
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Effects of waste frying oil based methyl and ethyl ester biodiesel fuels on the performance, combustion and emission characteristics of a DI diesel engine

TL;DR: In this article, fuel quality biodiesels produced from waste frying oil using methanol and ethanol were tested as pure and 20% (v/v) blend with petroleum-based diesel fuel (PBDF) in a direct injection (DI) diesel engine running at 600 nm and three different engine speeds (1100, 1400 and 1700 nm).
Journal ArticleDOI

A comprehensive review on biodiesel purification and upgrading

TL;DR: A comprehensive overview on the techniques and methods used for biodiesel purification and upgrading can be found in this article, where the authors classified the purification methods into equilibrium-based, affinitybased, membrane-based and reaction-based processes.
Journal ArticleDOI

Integrated production of biodiesel and bioethanol from sweet potato.

TL;DR: In this article, the production of sweet potato bioethanol was conducted at a small industrial plant in Brazil and integrated in biodiesel production through ethanolysis, with focus on biodiesel yield and purity.
Journal ArticleDOI

Biodiesel dry purification with sugarcane bagasse

TL;DR: In this article, the application of sugarcane bagasse as a low-cost adsorbent material for biodiesel treatment was proposed, and the results showed that the addition of only 0.5% of sugar cane bagasse removed 40% of the glycerine of the crude biodiesel and produced a purified biodiesel with less than 0.02% of glycerin.
Journal ArticleDOI

Chamotte clay as potential low cost adsorbent to be used in the palm kernel biodiesel purification

TL;DR: In this article, a face centered composite design was used to analyze the combined effect of chamotte concentration and temperature on glycerol removal, which indicated that the rate-limiting step may be chemisorption.
References
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Journal ArticleDOI

Production of biodiesel from acid waste lard

TL;DR: The proposed pre-treatment was effective to enable acid wastes as single raw materials for biodiesel production with acceptable quality; however, low yields were obtained and alkali transesterification of a mixture of waste lard and soybean oil resulted in a product with a purity of 99.8 wt%, showing that blending might be an interesting alternative to recycle such wastes.
Journal ArticleDOI

Preparation of biodiesel from waste oils catalyzed by a Brønsted acidic ionic liquid

TL;DR: Preparation of biodiesel from waste oils catalyzed by a novel Brønsted acidic ionic liquid with an alkane sulfonic acid group had a good reusability and can be easily separated from the biodiesel by simple decantation.
Journal ArticleDOI

Refining of biodiesel by ceramic membrane separation

TL;DR: In this article, a ceramic membrane separation process for biodiesel refining was developed to reduce the considerable usage of water needed in the conventional water washing process, which was a potential environmental process for the refining of biodiesel.
Journal ArticleDOI

Separation of biodiesel and glycerol using ceramic membranes

TL;DR: In this paper, the efficiency of microfiltration with ceramic membranes in the separation of biodiesel and glycerol was investigated, and the best performance was obtained with the 0.2μm membrane and 2.0bar transmembrane pressure.
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Frequently Asked Questions (12)
Q1. What are the contributions mentioned in the paper "Study of an ethylic biodiesel integrated process: raw-materials," ?

In this paper, a transesterification reaction is reversible and involves three steps to convert the initial triglyceride into a mixture of biodiesel and the by-product glycerol. 

Vegetable food oils, such as soybean 46 oil, rapeseed oil, palm oil and sunflower oil are used in more than 95 % of biodiesel 47 production plants throughout the world [4]. 

57 Virgin vegetable oils might account for up to 95% of the biodiesel production costs [6]; 58 therefore, raw-material diversification might have significant impact on improving the 59 economic viability of the process. 

In order to evaluate the biodiesel production process, 14 preliminary experiments were 218 conducted, by varying the reaction temperature, time, ethanol:oil molar ratio and 219 homogeneous catalyst (NaOH) concentration aiming to select the best conditions to 220 obtain high conversion and identify key reaction parameters. 

The 417 membrane purified product presented 69 ppm of Na, whereas the product purified with 418 the resin presented 108 ppm of Na. 

351 Taking into account the results obtained during preliminary studies and also that the use 352 of high alcohol:oil molar ratios in the transesterification reaction is known to 353 significantly increase separation and purification costs [20], the optimized conditions 354 were selected as 45 ºC and 6:1 ethanol to oil molar ratio. 

Taking into account the great amount of work on ethanolysis 230conducted at 80 C, initially, experiments were conducted at that temperature and by 231varying the ethanol:oil molar ratio, the catalyst concentration and the reaction time. 

The 319 experimental planning included performing all experiments in duplicate except for the 320 central point that was performed in triplicate (19 experiments were performed). 

It can be seen that, using a 9:1 ethanol:oil molar 326 ratio, minor effects were found on varying the temperature; in this case, the purity was, 327 in average 92.3 ± 0.7 and the viscosity 4.76 ± 0.04 mm2 s-1. 328 When using 6:1 and also when using 12:1 ethanol:oil molar ratio, a more significant 329 effect was found by varying the temperature, with the highest purity being obtained at 330 40 ºC and 6:1 ethanol:oil molar ratio and at 30 ºC, using 12:1, being in both cases very 331 similar (close to 96 wt.%). 

The results showed that to achieve high 449 conversions at a relatively low temperature, of 30 ºC, a high ethanol:oil molar ratio is 450 required (12:1); on the other hand, no benefit results from increasing the temperature up 451 to 50 ºC using such a high ethanol:oil molar ratio. 

To do that, after 1 h 255 the reaction was stopped, the products were settled and glycerol was removed as 256 described in section 2.2.1. 

The ethanolic route is in fact 84 more promising; however, the process is much more sensitive and it still needs to be 85 optimized, namely regarding reaction conditions and product separation constraints, to 86 be competitive with the methanolic route [17].