1972
DOI: 10.1021/es60071a004
|View full text |Cite
|
Sign up to set email alerts
|

Desulfurization of fuels with half-calcined dolomite. First kinetic data

Abstract: w Kinetic data are given for the first time for reaction of half-calcined dolomite with H2S (55O-80O0C, 0.005-0.2 atm of H2S in gas at 1 atm). The reaction can be used to remove H2S from a fuel gas made by gasifying coal with air and steam at high pressure. Gas at 20 atm from a dilute-phase slagging gasifier can be desulfurized in an operation at about 920°C to reduce the SO2 emission from power generation to roughly that expected from coal containing 0.15 sulfur. Gas at 20 atm from an ash-agglomerating fluidi… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1
1
1

Citation Types

3
49
0

Year Published

1980
1980
2000
2000

Publication Types

Select...
4
3
3

Relationship

0
10

Authors

Journals

citations
Cited by 58 publications
(52 citation statements)
references
References 3 publications
(3 reference statements)
3
49
0
Order By: Relevance
“…Many studies of the reaction between calcined limestone (CaO) and half or fully calcined dolomites (respectively CaC0 3 -Mg0 and CaO-MgO) with HzS have been published (Abbasian et al, 1990;Freund, 1981;Squires et al, 1971;Ruth et al, 1972;Yen, 1979). These works were often concerned with the addition of limestone or dolomite to the coal in the gasifier where the conditions are such that the calcination of the calcium carbonate or the magnesium carbonate might occur rapidly (Freund, 1981), or were conducted at a C0 2 fugacity low enough to obtain partial or total calcination of the calcium carbonate.…”
Section: Chapi'er 2: Previous Workmentioning
confidence: 99%
“…Many studies of the reaction between calcined limestone (CaO) and half or fully calcined dolomites (respectively CaC0 3 -Mg0 and CaO-MgO) with HzS have been published (Abbasian et al, 1990;Freund, 1981;Squires et al, 1971;Ruth et al, 1972;Yen, 1979). These works were often concerned with the addition of limestone or dolomite to the coal in the gasifier where the conditions are such that the calcination of the calcium carbonate or the magnesium carbonate might occur rapidly (Freund, 1981), or were conducted at a C0 2 fugacity low enough to obtain partial or total calcination of the calcium carbonate.…”
Section: Chapi'er 2: Previous Workmentioning
confidence: 99%
“…As the equilibrium constant for reaction (2) is seen to be several orders of magnitude larger than for reaction (3), it may be inferred that reaction (2) is the main gas/solid reaction involved in the regeneration of CaS by CO 2, Further, the equilibrium constant for reaction (4) is in turn larger than that for reaction (2) by several orders of magnitude. Under the conditions, for example, at high temperatures, where chemical reaction is not controlling, the gas-phase at the reaction site is likely to be at equilibrium with respect to reaction (2) and (3).…”
Section: Chemistry and Thermodynamicsmentioning
confidence: 94%
“…In view of this difference, the information that is presently available on the sulfidation of limestone-derived calcines (e.g., see and Efthimiadis and Sotirchos (1992)) and sulfidation of half-calcined dolomites (e.g., see Ruth et al (1972) and Yen et al (1981)) from studies in thermogravimetric analysis (TGA) systems and other types of reactors is inapplicable to the direct reaction of limestones with H 2 S. Few fundamental studies have been presented in the literature on the direct reaction of limestones with H 2 S, and most of those have been carried out under low pressures or under conditions where both sulfidation reactions ( (7) and (8)) could take place (Attar and Dupuis, 1979). …”
Section: Background Informationmentioning
confidence: 99%