Hydrodemetalation and hydrodesulfurization using a catalyst of specified macroporosity.
作者： David R. Johnson
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摘要: For a heavy hydrocarbonaceous feed, especially good hydrodemetalation and hydrodesulfurization are achieved, as well MCR reduction, using catalyst having 5 to 11 percent of its pore volume in the form macropores, surface area greater than 75 m2/g. Preferably has peak mesopore diameter 165A, determined by mercury porosimetry, an average 160A.
lens.org 参考文章(19)
Albert L. Hensley, April J. Evans, William I. Beaton, Catalyst for demetallation and desulfurization of heavy hydrocarbons ,(1987)
Geoffrey R Wilson, Heavy oil demetallization and desulfurization process ,(1973)
K Riley, W Sawyer, Hydrodesulfurization with a specified pore size distribution in silica-stabilized alumina ,(1970)
Ralph J. Bertolacini, L. Charles Gutberlet, Dae K. Kim, Ken K. Robinson, Process for coal liquefaction and catalyst ,(1979)
Thomas R. Stein, Edward J. Rosinski, Ronald H. Fischer, Catalyst for residua demetalation and desulfurization ,(1973)
Shigeo Utsumi, Polyethylene-2,6-naphthalate film for capacitor ,(1986)
Jose E. Herrera, Moises G. Sanchez, Extruded alumina catalyst support having controlled distribution of pore sizes ,(1980)
Albert L. Hensley, Leonard M. Quick, Process for demetallation and desulfurization of heavy hydrocarbons ,(1985)
Albert L. Hensley, Lawrence B. Peck, George L. Ott, Process for the hydrodemetallation hydrodesulfuration and hydrocracking of a hydrocarbon feedstock ,(1987)
Harvey D. Schindler, Hydrotreating catalyst and use thereof ,(1983)