1992
DOI: 10.1021/ie00006a023
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Hydrodesulfurization of sulfur-containing polyaromatic compounds in light oil

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Cited by 271 publications
(130 citation statements)
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“…The condensed thiophenes are the most common forms in which sulfur is present (28). Alkyl DBTs and alkyl BTs are highly recalcitrant to chemical catalysts, especially when alkylated at the 4 and 6 positions (9,14,20). Many research efforts have been put into the investigation of biological desulfurization systems using DBTs or alkylated DBTs as model compounds, and the metabolic pathway of desulfurization has been proposed as the so-called "4S" or extended "4SM" pathway (5,7,12,16,18).…”
mentioning
confidence: 99%
“…The condensed thiophenes are the most common forms in which sulfur is present (28). Alkyl DBTs and alkyl BTs are highly recalcitrant to chemical catalysts, especially when alkylated at the 4 and 6 positions (9,14,20). Many research efforts have been put into the investigation of biological desulfurization systems using DBTs or alkylated DBTs as model compounds, and the metabolic pathway of desulfurization has been proposed as the so-called "4S" or extended "4SM" pathway (5,7,12,16,18).…”
mentioning
confidence: 99%
“…Figure 9 shows GC-FPD chro matograms of the oil layers before and after oxidation. Most sulfur-containing compounds present in SR-LGO are alkyl-substituted BTs and alkyl-substituted DBTs 70) . The GC peaks of sulfur compounds in oil layers of oxidized samples were shifted in the heavier molecular weight direction, indicating formation of the corre sponding sulfones, as shown in Fig.…”
Section: Oxidation Of Straight Run Light Gas Oil Withmentioning
confidence: 99%
“…First, we found that during preparation the textural and physical properties of the sol-gel Al 2 O 3 4 powders can be finely tuned by changing the ratio of hydrolysis (R), defined as [H 2 O]/[aluminum-tri-sec-butoxide (ASB)] [29]. Then, we showed that the HDS performance of CoMo catalysts supported on sol-gel prepared Al 2 O 3 powders depend on R. The catalytic activities were maximal for R = 8 ~ 10 and superior to that of an industrial reference catalyst (IRC) for HDS of thiophene and dibenzothiophene (DBT), whereas inferior to the IRC for HDS of 4,6-dimethyldibenzothiophene (4,6-DMDBT) [31], which is well known as one of the most HDS-refractory compounds present in diesel oil fractions [32,33]. That particular study also showed that HDS of 4,6-DMDBT requires the hydrogenation (HYD) of 4H-4,6-DMDBT to 6H-4,6-DMDBT, which is promoted over catalysts with R = 8 ~ 10 that exhibit the largest proportion of strong acid sites relative to the total quantity of acid sites [31].…”
Section: Al 2 O 3 Based Supports and Enhancement Of The Catalytic Funmentioning
confidence: 99%