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desulfurization

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Series: ASM Handbook
Volume: 13C
Publisher: ASM International
Published: 01 January 2006
DOI: 10.31399/asm.hb.v13c.a0004153
EISBN: 978-1-62708-184-9
... Abstract This article begins with a discussion on the components and importance of flue gas desulfurization (FGD) technology used in power plant for pollution control. It further discusses the corrosion problems encountered in different operating zones of FGD system and the major forms...
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Published: 01 January 2002
Fig. 26 Cracks in naphtha desulfurization reactor attributed to hydrogen damage. (a) Note decarburized region adjacent to crack. 25×. (b) Higher-magnification view. 200× More
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Published: 30 August 2021
Fig. 99 Cracks in naphtha desulfurization reactor attributed to hydrogen damage. (a) Note decarburized region adjacent to crack. Original magnification: 25×. (b) Higher-magnification view. Original magnification: 200× More
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Published: 01 January 1990
Fig. 18 Pitting of type 316L stainless steel in flue gas desulfurization scrubber environments. Solid lines indicate zones of differing severity of corrosion; because the zones are not clearly defined, the lines cannot be precisely drawn. Source: Ref 52 More
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Published: 09 June 2014
Fig. 18 Desulfurization in the through-flow process More
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Published: 09 June 2014
Fig. 22 Desulfurization and cleaning steel melts by slag reaction with simultaneous argon flushing in a medium frequency (induction furnace. Source: Ref 27 More
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Published: 01 December 2008
Fig. 1 Weight fraction desulfurizer required to achieve given desulfurization ratios. Plots for electric-melted iron and steel (curve A) assume initial sulfur concentrations [%(S) i = 0.03] different from those of cupola-melted iron [(%S) i = 0.10] (curve B). More
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Published: 01 December 2008
Fig. 2 Desulfurization ratio-basicity comparisons for cupola (closed circles) and laboratory data (open circles). Equilibrium values are indicated by the angled line. The vertical line indicates the slag basicity above which slags are saturated at 1500 °C (2730 °F), with respect to dicalcium More
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Published: 01 December 2008
Fig. 3 Slag sulfide capacities, oxygen activities, and desulfurization ratios, measured and calculated, for a cupola operated with municipal ferrous refuse as a charge material. Source: Ref 8 More
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Published: 01 December 2008
Fig. 4 Equilibrium sulfur concentrations for CaO desulfurization calculated with Eq 11 and 12 , assuming a CaO = a CaS = a SiO 2 = 1. Source: Ref 2 More
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Published: 01 December 2008
Fig. 6 Desulfurization rates of carbon-saturated iron, containing 0.4% Si, with CaO and varying amounts of CaF 2 at 1450 °C (2640 °F). Source: Ref 9 More
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Published: 01 December 2008
Fig. 7 Dependence of CaO desulfurization rate constant on the rate of gas flow through a reactor. Source: Ref 16 More
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Published: 31 August 2017
Fig. 23 Weight ratio desulfurizer required to achieve given desulfurization ratios. Plots for electric-melted iron and steel (line A) assume initial sulfur concentration (%S) i = 0.03, different from that of cupola-melted iron (line B) at (%S) i = 0.01. Source: Ref 35 More
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Published: 31 August 2017
Fig. 24 Desulfurization rates of carbon-saturated iron, containing 0.4% Si, with CaO and varying amounts of CaF 2 at 1450 °C (2640 °F). Source: Ref 42 More
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Published: 01 January 1997
Fig. 8 The effect of desulfurization (1280 °C, or 2335 °F, 100 h hydrogen anneal) or yttrium additions (100–150 ppm) on the 1150 °C (2100 °F) cyclic oxidation behavior of René N5. Source: Ref 8 More
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Published: 01 January 2005
Fig. 16 Pitting of type 316L stainless steel in flue gas desulfurization scrubber environment. Solid lines indicate zones of differing severity of corrosion; because the zones are not clearly defined, the lines cannot be precisely drawn. Source: Ref 39 More
Book: Casting
Series: ASM Handbook
Volume: 15
Publisher: ASM International
Published: 01 December 2008
DOI: 10.31399/asm.hb.v15.a0005190
EISBN: 978-1-62708-187-0
... Abstract This article addresses two issues on thermodynamics, namely, the calculation of solubility lines and the calculation of the activity of various components. It discusses alloying elements in terms of their influence on the activity of carbon. The article describes the desulfurization...
Series: ASM Handbook
Volume: 4C
Publisher: ASM International
Published: 09 June 2014
DOI: 10.31399/asm.hb.v04c.a0005903
EISBN: 978-1-62708-167-2
... Abstract Interplays of metallurgical factors, such as dissolved oxygen, carbon, and silicon content, that control the molten metal from melting to pouring, have a decisive influence on the quality of the castings. This article focuses on the magnesium treatment and desulfurization carried out...
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Published: 01 January 1990
Fig. 31 Effect of temperature and hydrogen sulfide content on high-temperature H 2 S/H 2 corrosion of (a) carbon steel, (b) 5Cr-0.5Mo steel, and (c) 9Cr-1Mo steel. These corrosion rates are based on the use of gas oil desulfurizers; corrosion rates with naphtha desulfurizers may be slightly More
Series: ASM Handbook
Volume: 13C
Publisher: ASM International
Published: 01 January 2006
DOI: 10.31399/asm.hb.v13c.a0004137
EISBN: 978-1-62708-184-9
... Abstract Corrosion problems and materials selection for emissions control equipment can be difficult because of varied corrosive compounds present and the severe environments encountered. This article discusses the selection of materials for construction of flue gas desulfurization systems...