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Hydrotreating, of petroleum

The red tetrathiomolybdate ion appears to be a principal participant in the biological Cu—Mo antagonism and is reactive toward other transition-metal ions to produce a wide variety of heteronuclear transition-metal sulfide complexes and clusters (13,14). For example, tetrathiomolybdate serves as a bidentate ligand for Co, forming Co(MoSTetrathiomolybdates and their mixed metal complexes are of interest as catalyst precursors for the hydrotreating of petroleum (qv) (15) and the hydroHquefaction of coal (see Coal conversion processes) (16). The intermediate forms MoOS Mo02S 2> MoO S have also been prepared (17). [Pg.470]

Molybdenum compounds Hydrodesulphurization and hydrotreating of petroleum Oxidation of methanol to formaldehdye Epoxidation of olefins Decomposition of alkali metal nitrides Irritation of eyes and respiratory tract Pneumoconiosis... [Pg.121]

This section covers recent advances in the application of three-phase fluidization systems in the petroleum and chemical process industries. These areas encompass many of the important commercial applications of three-phase fluidized beds. The technology for such applications as petroleum resid processing and Fischer-Tropsch synthesis have been successfully demonstrated in plants throughout the world. Overviews and operational considerations for recent improvements in the hydrotreating of petroleum resids, applications in the hydrotreating of light gas-oil, and improvements and new applications in hydrocarbon synthesis will be discussed. [Pg.614]

Hydrotreating of petroleum feedstocks have become more and more crucial not only for protecting environments but also for efficient utilization of natural resources. Extensive researches have been conducted to develop highly active catalysts for hydrotreating, in particular for hydrodesulfurization (HDS) [1-3]. [Pg.77]

In petroleum hydrotreating, both vapor phase and trickle bed reactors are used for catalytic hydrotreating of petroleum fractions. Under normal processing conditions, naphthas are completely in the vapor phase while higher boiling fractions are hydrotreated in a mixed-phase trickle bed reactor. These two types of catalytic reactors are discussed extensively. [Pg.2567]

A stripped RD column could be applied in the hydrocracking and hydrotreating of petroleum to avoid excessive hydrocracking or hydrotreating of lighter products. " If the desired products are of higher molecular weight, a rectified RD column can be used. [Pg.2606]

Molybdenum sulfide-based catalysts are widely used in heterogeneous catalysis, especially in hydrotreating of petroleum cuts. The control of the morphology and size of MoSx nanoparticles is thus of great interest to obtain highly active and selective catalysts [1], Various methods have been used to synthesize nanoparticles with controlled morphology and structure, and the use of microemulsions seems especially suited for tailoring particle size at the nanolevel [2]. [Pg.239]

Older rerefining units used 2-5 kg/L of activated clay at 40—70°C and higher temperatures in place of TEE to clean the oil (80). More elaborate chemical and hydrotreating of used engine oils without a distillation step has been developed by Phillips Petroleum for processing 40,000 /yr (10 X 10 gal/yr). Establishment of a reflable feedstock supply is a critical consideration for larger rerefining plants. [Pg.256]

In most applieations, the reaetion oeeurs between a dissolved gas and a liquid-phase reaetant in the presenee of a solid eatalyst. In some eases, the liquid is an inert medium and the reaetion takes plaee between the dissolved gases at the solid surfaee. These reaetors have many diverse applieations in eatalytie proeesses and are used extensively in the ehemieal industry. Triekle-bed reaetors have been developed by the petroleum industry for hydrodesulfurization, hydroeraeking, and hydrotreating of various petroleum fraetions of relatively high boiling point. Under reaetion eonditions, the hydroearbon feed is frequently a vapor-liquid mixture that reaets at liquid hourly spaee veloeities (LHSV in volume of fresh feed, as liquid/volume of bed, hr) in the... [Pg.241]

Marchal, N. Kasztelan, S., and Mignard, S., A comparative study of catalysts for the deep aromatic reduction in hydrotreated gas oil. In Catalytic Hydroprocessing of Petroleum and Distillates, M.C. oballa, S.S.S. editor. 1994, Marcel Dekker New York. pp. 315-327. [Pg.60]

Hyd rofining A process for desulfurizing and hydrotreating a wide range of petroleum fractions. Licensed by the Esso Research and Engineering Company. [Pg.138]

Trickle-bed reactors are used in catalytic hydrotreating (reaction with H2) of petroleum fractions to remove sulfur (hydrodesulfurization), nitrogen (hydrodenitrogena-tion), and metals (hydrodemetallization), as well as in catalytic hydrocracking of petroleum fractions, and other catalytic hydrogenation and oxidation processes. An example of the first is the reaction in which a sulfur compound is represented by diben-zothiophene (Ring and Missen, 1989), and a molybdate catalyst, based, for example, on cobalt molybdate, is used ... [Pg.619]

Assuming that demand for petroleum continues to increase at a rate of 1.2% per annum to 2010,37 and that all gasoline and diesel produced by U.S. refineries will have a sulfur content of less than 30 ppm, desulfurization of gasoline and diesel to these low levels will require extensive hydrotreating of both catalytic cracker feed and product of distillate. [Pg.28]

Brossard, D.N. (1997) Chevron RDS/ VRDS hydrotreating-transportation fuels from the bottom of the barrel, in Handbook of Petroleum Refining Processes, 2nd edn (ed. R.A. Myers), McGraw-Hill, pp. 8.3-8.26... [Pg.400]

The stability of the products from coal-derived syncrudes must be examined carefully. Many unique compounds are present in these syncrudes peri-condensed aromatics and naphthenes, oxygen compounds, and asphaltene-like hydrocabons. Traces of these compounds may remain in the hydrotreated product and their effect on jet, thermal, and oxidation stabilities cannot be predicted from the behavior of petroleum products. [Pg.138]

The estimation of 1.109t/year of petroleum or substitutes to be hydrotreated... [Pg.147]


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See also in sourсe #XX -- [ Pg.85 , Pg.86 , Pg.87 , Pg.88 ]




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