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Marija R. Miladinović

Researcher at University of Niš

Publications -  20
Citations -  710

Marija R. Miladinović is an academic researcher from University of Niš. The author has contributed to research in topics: Biodiesel & Biodiesel production. The author has an hindex of 10, co-authored 16 publications receiving 517 citations. Previous affiliations of Marija R. Miladinović include University of Belgrade.

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Calcium oxide as a promising heterogeneous catalyst for biodiesel production: Current state and perspectives

TL;DR: In this paper, an overview of the recent progress in the development of various CaO-based catalysts suitable for biodiesel production is presented, where the mechanism, kinetics and optimization of transesterification reaction over these catalysts are first considered.
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Application of nano CaO–based catalysts in biodiesel synthesis

TL;DR: An overview of the preparation of nano-sized CaO-based catalysts and their application in the biodiesel production is given in this article, where the authors prove the promising potentiality of nano CaO−based catalyst as solid catalysts in biodiesel.
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Valorization of walnut shell ash as a catalyst for biodiesel production

TL;DR: In this article, the authors investigated the catalytic activity of the walnut shell ash in the biodiesel production by the sunflower oil methanolysis and found that it provided a very fast reaction and a high FAME content (over 98%).
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A kinetic study of quicklime-catalyzed sunflower oil methanolysis

TL;DR: In this paper, the quicklime-catalyzed sunflower oil methanolysis was studied at mild reaction conditions and the optimal methanol-to-oil molar ratio and quicklime amount for achieving the highest fatty acid methyl esters content were established to be 12:1 and 5%, respectively.
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Modeling and optimization of sunflower oil methanolysis over quicklime bits in a packed bed tubular reactor using the response surface methodology

TL;DR: In this article, the effect of the residence time (i.e., liquid flow rate through the reactor), methanol-to-oil molar ratio and reaction temperature on the fatty acid methyl esters (FAMEs) content at the output of a continuous packed bed tubular reactor was modeled by the response surface methodology (RSM) combined with the 33 full factorial design (FFD) with replication or the Box-Behnken design (BBD) with five center points.