Cosmo Oil Co., Ltd.

Other

Petroleum Energy Center

Cosmo Research Institute

Yasuo Yamamoto

Yukio Shibata

Yoshihiro Mizutani

Kazushi Usui

Tomohiro Yoshinari

Hatsutaro Yamazaki

Mitsuru Ohi

Takeshi Tomino

Keizou Nagata

A hydrotreating catalyst for heavy hydrocarbon oil, which comprises a boron-containing alumina carrier containing from 1 to 12 wt %, in terms of an oxide, of boron based on the catalyst, having supported thereon a metal in the Group VI, wherein the catalyst has an average pore size of from 19 to 25 nm, a pore volume of from 0.65 to 0.8 ml/g, a catalyst strength of 3 lb/mm or more, and a specific surface area of from 70 to 130 m,/g; a process for producing the hydrotreating catalyst; and a method for hydrotreating heavy hydrocarbon oil, which comprises conducting a catalytic reaction of heavy hydrocarbon oil in the presence of the catalyst composition at a temperature of from 300 to 500&deg; C., a pressure of from 3 to 20 MPa, a hydrogen/oil ratio of from 400 to 3000 Nl/l, and LHSV of from 0.1 to 1.5 hr,.

Hydrotreating catalyst for heavy hydrocarbon oil, process for producing the catalyst, and hydrotreating method using the same

Disclosed is a process for hydroconverting a heavy hydrocarbon oil in a reactor under high-temperature and high-pressure conditions, wherein said hydroconversion is carried out through using at least three desulfurization catalysts which each contains as active metals transition metals of Group VI and VIII in the Periodic Table supported on an alumina carrier and which have different SI of 40 or higher, 30 or higher and below 40, and lower than 30, respectively, and wherein said at least three catalysts are packed into the reactor in a descending order of SI from the inlet to the outlet of the reactor, with the proportion of the catalyst having SI of 40 or higher is at least 10% by volume, that of the catalyst having SI of 30 or higher and below 40 is at least 20% by volume, and that of the catalyst having SI of lower than 30 is at least 30% by volume.

Hydroconversion process for heavy hydrocarbon oil

A catalyst composition for the hydrotreatment of hydrocarbon oils is disclosed. The composition comprises at least one metal compound having hydrogenating activity belonging to a Group VIB or Group VIII carried on a carrier comprising 2-35% by weight of zeolite and 98-65% by weight of alumina or an alumina-containing substance, wherein, (A) said alumina or alumina-containing substance (1) has a mean pore diameter of 60-125 angstrom and (2) contains the pore volume of which the diameter falls within .+-.10 angstrom of the mean pore diameter of 70-98% of the total pore volume, (B) said zeolite (3) has a mean particle size of 6 .mu.m or smaller and (4) contains particles of which the diameter is 6 .mu.m or smaller of 70-98% of all zeolite particles. It has both high hydrodesulfurization and high cracking capabilities at the same time, and can selectively crack the heavy fractions which have once been hydrotreated, yielding lighter fractions.

Catalyst composition for hydrotreating of hydrocarbons and hydrotreating

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Saitama, Japan

Yasuo Yamamoto