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<ArticleSet>
<Article>
<Journal>
				<PublisherName>Arak University</PublisherName>
				<JournalTitle>Colloid &amp;  Nanoscience  Journal</JournalTitle>
				<Issn>2980-9215</Issn>
				<Volume>3</Volume>
				<Issue>1</Issue>
				<PubDate PubStatus="epublish">
					<Year>2025</Year>
					<Month>04</Month>
					<Day>01</Day>
				</PubDate>
			</Journal>
<ArticleTitle>Integration of deasphalting and oxidative desulfurization processes for heavy fuel oil desulfurization</ArticleTitle>
<VernacularTitle></VernacularTitle>
			<FirstPage>563</FirstPage>
			<LastPage>571</LastPage>
			<ELocationID EIdType="pii">729740</ELocationID>
			
<ELocationID EIdType="doi">10.61882/CNJ.3.1.563</ELocationID>
			
			<Language>EN</Language>
<AuthorList>
<Author>
					<FirstName>Reza</FirstName>
					<LastName>Mokhtar</LastName>
<Affiliation>Department of Chemical Engineering, Faculty of Engineering, Arak University, Iran</Affiliation>

</Author>
<Author>
					<FirstName>Samaneh</FirstName>
					<LastName>Bandehali</LastName>
<Affiliation>Department of Mechanical Engineering, Ayatollah Boroujerdi University, Iran</Affiliation>

</Author>
</AuthorList>
				<PublicationType>Journal Article</PublicationType>
			<History>
				<PubDate PubStatus="received">
					<Year>2025</Year>
					<Month>07</Month>
					<Day>26</Day>
				</PubDate>
			</History>
		<Abstract>In this study, a combined process consisting of solvent de-asphalting followed by continuous ultrasound-assisted oxidative desulfurization (UAOD) was applied for the treatment of heavy fuel oil (HFO). Acetic acid (99 wt.%) and hydrogen peroxide (35 vol.%) were employed as the catalyst and oxidant, respectively. n-Heptane and n-hexane were tested as de-asphalting solvents, while methanol and acetonitrile were used as extraction solvents in the liquid–liquid separation stage. The integrated process exhibited high efficiency in sulfur removal, reducing the sulfur content of HFO to below 5000 ppm. The most effective performance was obtained when n-heptane was used for de-asphalting, combined with ultrasonic desulfurization and subsequent extraction with methanol, which lowered the sulfur content to approximately 5292 ppm.</Abstract>
		<ObjectList>
			<Object Type="keyword">
			<Param Name="value">De-asphalting</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Ultrasonic- assisted oxidative desulfurization (UAOD)</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Sulfur Removal</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Oxidative</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">heavy fuel oil (HFO)</Param>
			</Object>
		</ObjectList>
<ArchiveCopySource DocType="pdf">https://cnj.araku.ac.ir/article_729740_b77fa228a4365e21924c0bbb0ac1c09d.pdf</ArchiveCopySource>
</Article>
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