2021
DOI: 10.1016/j.fuproc.2020.106701
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Dynamic hydrogen-intensified methanation of synthetic by-product gases from steelworks

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Cited by 15 publications
(21 citation statements)
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“…The authors concluded that a 4-5% H 2 surplus is required within the tested GHSV to achieve a full methane yield for a three-stage methanation setup outlined above. Hauser et al [26] reported the same value for a heat pipe cooled structured fixed-bed reactor. For the expression of the reaction stoichiometry, the parameter σ H 2 is introduced, which describes the ratio of the molar hydrogen flow to the molar flows of CO and CO 2 present in the feed gas (Equation ( 5)).…”
mentioning
confidence: 66%
“…The authors concluded that a 4-5% H 2 surplus is required within the tested GHSV to achieve a full methane yield for a three-stage methanation setup outlined above. Hauser et al [26] reported the same value for a heat pipe cooled structured fixed-bed reactor. For the expression of the reaction stoichiometry, the parameter σ H 2 is introduced, which describes the ratio of the molar hydrogen flow to the molar flows of CO and CO 2 present in the feed gas (Equation ( 5)).…”
mentioning
confidence: 66%
“…Based on experimental results, the reaction mechanism is assumed to consist of a more complex reaction network, taking provision for the formation of solid carbon through the Boudouard reaction [37,38]. The methanation process is usually conducted at low pressures (<10 bar) with nickel-based catalysts as the main employed catalysts.…”
Section: Methanationmentioning
confidence: 99%
“…The methanation process is usually conducted at low pressures (<10 bar) with nickel-based catalysts as the main employed catalysts. The operating temperature is a crucial factor for catalyst lifetime and efficiency and could vary between 200 • C and 600 • C [36,38]. The stoichiometric number (SN) for methanation expresses the ratio between the added hydrogen and the carbonaceous components of the feed mixture and is expressed in molar flowrates:…”
Section: Methanationmentioning
confidence: 99%
“…These gases are usually exploited to meet the energy demand of production processes, to produce steam and as energy sources for power plants, which can both satisfy internal electricity demand and sell part of their production on the external energy market. An alternative way of utilizing off-gases is to exploit chemical synthesis reactors converting the carbon content to more valuable products, such as methane (CH 4 ) [36] and methanol (CH 3 OH), through the enrichment of by-product gases with H 2 . The project entitled "Integrated and intelligent upgrade of carbon sources through hydrogen addition for the steel industry" (i3upgrade), which is funded by Research Fund for Coal and Steel (RFCS) of European Union (EU), aims at efficiently managing process off-gases to increase the economic and environmental sustainability of the integrated steelworks production.…”
Section: Off-gases Management and Valorisation Through Hydrogen Enric...mentioning
confidence: 99%