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<rdf:RDF xmlns:rdf="http://www.w3.org/1999/02/22-rdf-syntax-ns#" xmlns:dc="http://purl.org/dc/elements/1.1/"><rdf:Description rdf:about="https://dk.um.si/IzpisGradiva.php?id=85069"><dc:title>Recovery of N-butanol from a complex five-component reactive azeotropic mixture</dc:title><dc:creator>Bogataj,	Miloš	(Avtor)
	</dc:creator><dc:creator>Kravanja,	Zdravko	(Avtor)
	</dc:creator><dc:creator>Nemet,	Andreja	(Avtor)
	</dc:creator><dc:subject>recycling</dc:subject><dc:subject>n-butanol</dc:subject><dc:subject>azeotropic mixture</dc:subject><dc:subject>separation</dc:subject><dc:subject>process design</dc:subject><dc:subject>energy efficiency</dc:subject><dc:description>This paper proposes a concept of a process design for the separation and recovery of n-butanol from a five-component mixture, consisting of n-butanol, isobutanol, formaldehyde, water and methanol. The mixture is a common waste stream in the production of butylated amino resins; therefore, recovery of n-butanol is crucial to the efficiency of the process. The results show that up to 94% of the n-butanol present in the waste stream can be recovered. Under the studied conditions, 99.76% pure n-butanol can be obtained, while formaldehyde, water and methanol are present only in traces. The energy intensity of the process is estimated at 2.42 MJ/kg of purified n-butanol. The economic analysis of the process shows that the process is economically viable over a wide range of production capacities, as evidenced by high net present values and high return on investment values.</dc:description><dc:publisher>MDPI AG</dc:publisher><dc:date>2022</dc:date><dc:date>2023-08-17 14:32:36</dc:date><dc:type>Znanstveno delo</dc:type><dc:identifier>85069</dc:identifier><dc:language>sl</dc:language><dc:rights>© 2022 by the authors</dc:rights></rdf:Description></rdf:RDF>
