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    Carbon-Dioxide and Hydrogen-Sulfide Removal from Simulated Landfill Gas Using Steel Slag

    Source: Journal of Environmental Engineering:;2020:;Volume ( 146 ):;issue: 012
    Author:
    Jyoti K. Chetri
    ,
    Krishna R. Reddy
    ,
    Dennis G. Grubb
    DOI: 10.1061/(ASCE)EE.1943-7870.0001826
    Publisher: ASCE
    Abstract: Municipal solid waste landfills are a source of major greenhouse gases such as methane (CH4) and carbon dioxide (CO2) and emit a trace amount of hydrogen sulfide (H2S). Recently, steel slag has extensively been used for mineral CO2 sequestration to minimize the CO2 releases to the atmosphere. This study explores the potential of basic oxygen furnace (BOF) steel slag to simultaneously remove CO2 and H2S from landfill gas (LFG). Various batch and column tests were conducted to evaluate the CO2 and H2S removal potential of the BOF slag under various conditions such as moisture content and particle size of the BOF slag. The three different particle sizes of BOF slag (coarse, as-is, and fine) were exposed to continuous flow of a synthetic LFG [50% CO2, 48.25% CH4, and 1.75% H2S by volume (v/v)] in a column reactor to evaluate the effect of particle size on CO2 and H2S removal capacity of the slag. Similarly, the BOF slag was exposed to synthetic LFG as well as 20% (v/v) of H2S alone in batch reactors at varying moisture contents (10%–30% by weight) to evaluate the effect of moisture content on the CO2 and H2S removal capacity of the slag. A significant H2S removal of 27  g H2S  kg−1 BOF slag and CO2 removal of 76 g CO2  kg−1 BOF slag were obtained in the batch reactor. The fine BOF slag (<0.106  mm) showed the maximum CO2 removal (300 g CO2  kg−1 BOF slag) and H2S removal (38 g H2S  kg−1 BOF slag) upon exposure to continuous synthetic LFG flow in the column reactor. The quantitative X-ray diffraction (QXRD) analysis showed the highest increase in carbon (77.5  g C  kg−1 BOF slag) and sulfur (28  g S kg−1 BOF slag) contents in the fine BOF slag, which was consistent with the mass balance of carbon and sulfur from CO2 and H2S uptake in column tests. The major reaction product with H2S was elemental sulfur depicted by the significant increase in the sulfur content in the X-ray fluorescence analysis. The key minerals involved in carbonation reactions were lime, portlandite, and larnite, as these minerals showed significant reduction in weight percentage (100%, 82%, and 80%, respectively) in the QXRD analysis. Overall, BOF slag showed promising results in mitigating CO2 and H2S from LFG.
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      Carbon-Dioxide and Hydrogen-Sulfide Removal from Simulated Landfill Gas Using Steel Slag

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    http://yetl.yabesh.ir/yetl1/handle/yetl/4268515
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    contributor authorJyoti K. Chetri
    contributor authorKrishna R. Reddy
    contributor authorDennis G. Grubb
    date accessioned2022-01-30T21:36:25Z
    date available2022-01-30T21:36:25Z
    date issued12/1/2020 12:00:00 AM
    identifier other%28ASCE%29EE.1943-7870.0001826.pdf
    identifier urihttp://yetl.yabesh.ir/yetl1/handle/yetl/4268515
    description abstractMunicipal solid waste landfills are a source of major greenhouse gases such as methane (CH4) and carbon dioxide (CO2) and emit a trace amount of hydrogen sulfide (H2S). Recently, steel slag has extensively been used for mineral CO2 sequestration to minimize the CO2 releases to the atmosphere. This study explores the potential of basic oxygen furnace (BOF) steel slag to simultaneously remove CO2 and H2S from landfill gas (LFG). Various batch and column tests were conducted to evaluate the CO2 and H2S removal potential of the BOF slag under various conditions such as moisture content and particle size of the BOF slag. The three different particle sizes of BOF slag (coarse, as-is, and fine) were exposed to continuous flow of a synthetic LFG [50% CO2, 48.25% CH4, and 1.75% H2S by volume (v/v)] in a column reactor to evaluate the effect of particle size on CO2 and H2S removal capacity of the slag. Similarly, the BOF slag was exposed to synthetic LFG as well as 20% (v/v) of H2S alone in batch reactors at varying moisture contents (10%–30% by weight) to evaluate the effect of moisture content on the CO2 and H2S removal capacity of the slag. A significant H2S removal of 27  g H2S  kg−1 BOF slag and CO2 removal of 76 g CO2  kg−1 BOF slag were obtained in the batch reactor. The fine BOF slag (<0.106  mm) showed the maximum CO2 removal (300 g CO2  kg−1 BOF slag) and H2S removal (38 g H2S  kg−1 BOF slag) upon exposure to continuous synthetic LFG flow in the column reactor. The quantitative X-ray diffraction (QXRD) analysis showed the highest increase in carbon (77.5  g C  kg−1 BOF slag) and sulfur (28  g S kg−1 BOF slag) contents in the fine BOF slag, which was consistent with the mass balance of carbon and sulfur from CO2 and H2S uptake in column tests. The major reaction product with H2S was elemental sulfur depicted by the significant increase in the sulfur content in the X-ray fluorescence analysis. The key minerals involved in carbonation reactions were lime, portlandite, and larnite, as these minerals showed significant reduction in weight percentage (100%, 82%, and 80%, respectively) in the QXRD analysis. Overall, BOF slag showed promising results in mitigating CO2 and H2S from LFG.
    publisherASCE
    titleCarbon-Dioxide and Hydrogen-Sulfide Removal from Simulated Landfill Gas Using Steel Slag
    typeJournal Paper
    journal volume146
    journal issue12
    journal titleJournal of Environmental Engineering
    identifier doi10.1061/(ASCE)EE.1943-7870.0001826
    page12
    treeJournal of Environmental Engineering:;2020:;Volume ( 146 ):;issue: 012
    contenttypeFulltext
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