2014
DOI: 10.1016/j.supflu.2014.01.016
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Conversion of sulfur-rich asphaltite in supercritical water and effect of metal additives

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Cited by 52 publications
(23 citation statements)
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“…Accordingly, a proper O2 amount is needed to guarantee the catalytic desulfurization of VR at a minimum expense cost. Apart what is listed above, the effect of metals (Zn, Al) [41,103] and catalysts (ZnO, MoO3 and MoS2) [12] on the desulfurization of heavy oil and model compounds in SCW have also been reported. Kida et al [75] proposed the reaction mechanism of hexyl sulfide (shown in Figure 7) in SCW, based on the analysis of experimental results and theory calculation.…”
Section: Removal Of Sulfurmentioning
confidence: 99%
“…Accordingly, a proper O2 amount is needed to guarantee the catalytic desulfurization of VR at a minimum expense cost. Apart what is listed above, the effect of metals (Zn, Al) [41,103] and catalysts (ZnO, MoO3 and MoS2) [12] on the desulfurization of heavy oil and model compounds in SCW have also been reported. Kida et al [75] proposed the reaction mechanism of hexyl sulfide (shown in Figure 7) in SCW, based on the analysis of experimental results and theory calculation.…”
Section: Removal Of Sulfurmentioning
confidence: 99%
“…Earlier we revealed that addition of zinc shavings to sulfur-rich asphaltite resulted in significant decrease in the amount of H 2 S in the volatile products during asphaltite pyrolysis in vacuum (T ≤ 400 • C) [15]. During conversion of bitumen [10], asphaltite [15] and coal [16] in supercritical water flow (400 • C, 30 MPa) the desulfurization degree (the weight portion of sulfur atoms of raw fuels passed into ZnS) of conversion products achieved 13, 60, and 42%, respectively.…”
Section: Introductionmentioning
confidence: 97%
“…Our interest in the study of zinc sulfidation is caused, first of all, by the possibility of using zinc for desulphurization and hydrogenation of low-grade fuels (oil shale [8], bitumen [9,10], oil sand bitumen [11], asphalt [12], asphaltite [13][14][15], and coal [16]) during their conversion in supercritical water (T cr = 374 • C, P cr = 22.1 MPa [17]). When zinc is added, hydrogenation of fuels is possible owing to hydrogen evolution during zinc oxidation by supercritical water [10,15,16].…”
Section: Introductionmentioning
confidence: 99%
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