“…Hitherto, Ni(Co)Mo(W)/γ-Al 2 O 3 is still the commercially and widespread employed HDS catalyst by virtue of its relatively high catalytic HDS activity, low price, outstanding stability, and peerless mechanical property. − However, it requires more stringent conditions, for instance, high operation temperature and H 2 pressure, for this kind of HDS catalysts to realize ultra-deep removal of intractable aromatic hydrocarbon compounds, such as 4,6-dimethyldibenzothiophene (4,6-DMDBT), and produce ultra-clean fuels conforming with the strict regulations and/or specifications of diesel quality from increasingly lower quality raw petroleum feed-stocks. − Accordingly, the design and construction of more efficient HDS catalyst is regarded as the straightforward yet desirable choice for the oil refining enterprises. Nowadays, there are mainly three strategies, involving reaction condition adjustment, − active phase modulation, − and support regulation, − reported in literature to enhance HDS performance of Ni(Co)Mo(W)/γ-Al 2 O 3 .…”