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            <title xml:lang="fr">Valorisation des fluides de coupe usés</title>
            <title xml:lang="fr" type="sub">Partie II : cas de l'évaporation à compression mécanique de vapeur</title>
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            <idno type="halRefHtml">&lt;i&gt;Environnement, Ingénierie &amp; Développement&lt;/i&gt;, 2004, N°36 - 4ème Trimestre 2004, pp.24-29. &lt;a target="_blank" href="https://dx.doi.org/10.4267/dechets-sciences-techniques.2152"&gt;&amp;#x27E8;10.4267/dechets-sciences-techniques.2152&amp;#x27E9;&lt;/a&gt;</idno>
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                <title xml:lang="fr">Valorisation des fluides de coupe usés</title>
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              <p>The cutting fluids produced by mechanical industrial processes are generally eliminated by evapo-incineration. The cost of treatment can be greatly reduced by simply extracting the water contained in the cutting fluids. Mechanical compressor evaporation has been studied with industrial microemulsion. The concentration factor has a value contained between 10 and 15 and the COD of distillate is near to 3 g/l. The COD is due to evaporation of fraction of basic oil. The economical analysis presents the financial viability of this process for evaporation of a volume of cutting fluids superior at 200 m3/year in actual conditions.</p>
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              <p>Des essais d'évaporation de fluides de coupe usés (microémulsion) ont été effectués à l'aide d'un évaporateur à compression mécanique de vapeur. Le facteur de concentration peut atteindre une valeur comprise entre 10 et 15. La DCO du distillat est voisine de 3 g/l, elle est due à l'évaporation d'une coupe d'huile provenant de l'huile de base de la microémulsion. Un calcul économique de ce procédé appliqué aux fluides de coupe montre que le temps de retour est d'environ 2,5 années pour un volume traité supérieur à 200 m3/an dans les conditions d'élimination actuelles.</p>
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