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Desulfurization of Hot Coal Gas by P. W. Sage (auth.), Aysel T. Atimtay, Douglas P. Harrison PDF

By P. W. Sage (auth.), Aysel T. Atimtay, Douglas P. Harrison (eds.)

ISBN-10: 3642589774

ISBN-13: 9783642589775

ISBN-10: 3642638104

ISBN-13: 9783642638107

Economic and environmental requisites for complex strength producing structures call for the removing of corrosive and different sulfurous compounds from scorching coal fuel. After a quick account of the realm power assets and an summary of unpolluted coal applied sciences, a evaluation of regenerable steel oxide sorbents for cleansing the new gasoline is equipped. Zinc oxide, copper oxide, calcium oxide, manganese oxide dependent in addition to supported and combined steel oxide sorbents are handled. functionality research of those sorbents, results of assorted parameters at the desulfurization potency, kinetics of sulfidation and regeneration reactions, sulfiding and regeneration mechanisms are mentioned. chapters current contemporary leads to the direct creation of elemental sulfur from regeneration or SO2-rich gases.

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This can be traced back to the early research and proving of pressurised fluidised bed combustion (PFBC) at the Coal Utilisation Research Laboratories (formerly BCURA) at Leatherhead, UK from the late I 960s through to the early 1980s. Larger scale work was undeltaken at the Grimethorpe PFBC during several operational phases from the late 1970s to the early 1990s[IO], culminating in the Grimethorpe Topping Cycle Project (GTCP) between 1990 and 1993. This joint prograrnme[ll] was the initial development of the Topping Cycle concept first proposed by British Coal in the 1970s.

1 compares the world total electricity generation (TEG) expressed as TeraWatt-hours (TWh) and world population for 1990 and the projections for the period 1990-2020. Most of the world total energy generation occurs in the highly industrialized regions of North America and Western Europe. The rest of the regions will have a moderate or a small growth rate. However, the absolute growth rate expressed as additional TWh produced, rather than percentages, is still the highest for the industrialized regions.

OXYGEN OR AIR MOVING BED II , - - / ... ASH AND CHAR FLUIDIZED BED GAS STEAM, OXYGEN OR AIR COAL SLAG SLAG ENTRAINED FLOW MOLTEN BATH Figure 5. Gasifier types: moving bed, fluidized bed, entrained flow, and molten bath 49 • • • Fluidized-bed gasifiers. These are subcategorized into non-agglomerating (H-T Winkler) and agglomerating (U-Gas, Kellog-Rust-Westinghouse (KRW» types. Both use dry feed of coal in the 1-5 mm size. Because lignites are very reactive, they are very suitable for fluidization in this type of gasifier.

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Desulfurization of Hot Coal Gas by P. W. Sage (auth.), Aysel T. Atimtay, Douglas P. Harrison (eds.)


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