Role of char during reburning of nitrogen oxides. Eighth quarterly report, July 1, 1995--September 30, 1995

Technical Report · Sun Nov 05 04:00:00 EST 1995

DOI:https://doi.org/10.2172/211510· OSTI ID:211510

Chen, Wei-Yin; Lu, Te-Chang ^[1]; Fan, L T; Yashima, Mutsuo ^[2]

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1. Mississippi Univ., University, MS (United States). Dept. of Chemical Engineering
2. Kansas State Univ., Manhattan, KS (United States). Dept. of Chemical Engineering

The investigation of this quarter focuses on the rates of NO reactions with chars in various gaseous environments. The results have revealed significant insights into the NO reduction mechanisms on char surface, particularly when the oxidants, O{sub 2} and CO{sub 2}, are introduced into the feed. Indeed, evidences suggest that the formation of stable oxygen complexes is the major cause of differences in NO reactivity on chars of different origins. The oxidants retard the reactivity of char derived fro the bituminous coal more seriously than they affect the char derived from lignite. Furthermore, additions of these oxidants into the reacting stream produce additional yields of CO and CO{sub 2} during NO reaction with lignite char, suggesting gasification of carbon from lignite char. No excess CO and CO{sub 2} were observed when the bituminous coal char was used. These yields of CO and CO{sub 2} also imply that desorption of stable surface oxygen complex is a rate-limiting step which may be catalyzed by the mineral matters during reactions involving lignite char. Surface area evaluated by CO{sub 2} and Dubinin-Radushkevich (D-R) equation is not a normalization factor of char reactivity during reburning. In the absence of oxidants, the bituminous coal char shows drastic increase in activation energy at about 950 {degrees}C indicating transition of desorption to adsorption controlled mechanisms. When CO{sub 2} is introduced, the transition temperature increases. When oxygen is also added, no such transition is observed up to 1100 {degrees}C. Lignite char reactivity increases smoothly over the temperature range 800 to 1100 {degrees}C. It is also observed that char reactivity decreases with increasing pyrolysis temperature which may be caused by closure of pores due to graphitization. The rate of NO reduction on the Pittsburgh {number_sign}8 coal char is then in good accord with that of a West Virginia coal char reported by De Soete (1980).

• Research Organization: Mississippi Univ., University, MS (United States). Dept. of Chemical Engineering
• Sponsoring Organization: USDOE, Washington, DC (United States)
• DOE Contract Number: FG22-93PC93227
• OSTI ID: 211510
• Report Number(s): DOE/PC/93227--T7; ON: DE96008833
• Country of Publication: United States
• Language: English

Related Subjects

01 COAL, LIGNITE, AND PEAT
BITUMINOUS COAL
CHARS
CHEMICAL REACTION KINETICS
COAL RANK
EXPERIMENTAL DATA
LIGNITE
NITROGEN OXIDES
OXIDIZERS
OXYGEN COMPLEXES
PROGRESS REPORT
REDUCTION
STAGED COMBUSTION
SURFACE AREA