110th Anniversary: Fluidized-Bed Chemical Reactors for Heterogeneously Catalyzed Gas–Solid Reactions: Old and New Applications
In this review, the potential of fluidized-bed technology for heterogeneously catalyzed gas–solid reactions is discussed. This reaction class can be divided into three reaction categories: gas-to-solid (G2S), solid-to-gas (S2G), and solid-to-gas-to-gas (S2G2G). The established examples of G2S reacti...
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Veröffentlicht in: | Industrial & engineering chemistry research 2019-11, Vol.58 (47), p.21173-21186 |
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description | In this review, the potential of fluidized-bed technology for heterogeneously catalyzed gas–solid reactions is discussed. This reaction class can be divided into three reaction categories: gas-to-solid (G2S), solid-to-gas (S2G), and solid-to-gas-to-gas (S2G2G). The established examples of G2S reactions are the gas-phase polymerizations of ethylene and propylene. However, other concepts, such as polymerization to butadiene rubber and synthesis of carbon nanotubes, are also discussed. It is a common feature of this reaction class that the catalyst remains a residue in the product and can influence its quality. S2G reactions are represented on a large scale by the synthesis of organosilanes. Another example is given by the hydrochlorination of silicon. In this reaction class, a particulate catalyst is anchored to the surface of the fluidized particles and should not be lost during the progressive conversion of the substrate. The fluidized-bed reactor is also suitable for performing the S2G2G reactions. Catalytic pyrolysis of biomass or waste is a good example of this class. In the first step, solid particles are thermally decomposed to gas and solid residue. In a consecutive step, gas released during pyrolysis is catalytically converted to value-added products. |
doi_str_mv | 10.1021/acs.iecr.9b03515 |
format | Article |
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This reaction class can be divided into three reaction categories: gas-to-solid (G2S), solid-to-gas (S2G), and solid-to-gas-to-gas (S2G2G). The established examples of G2S reactions are the gas-phase polymerizations of ethylene and propylene. However, other concepts, such as polymerization to butadiene rubber and synthesis of carbon nanotubes, are also discussed. It is a common feature of this reaction class that the catalyst remains a residue in the product and can influence its quality. S2G reactions are represented on a large scale by the synthesis of organosilanes. Another example is given by the hydrochlorination of silicon. In this reaction class, a particulate catalyst is anchored to the surface of the fluidized particles and should not be lost during the progressive conversion of the substrate. The fluidized-bed reactor is also suitable for performing the S2G2G reactions. Catalytic pyrolysis of biomass or waste is a good example of this class. 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Eng. Chem. Res</addtitle><description>In this review, the potential of fluidized-bed technology for heterogeneously catalyzed gas–solid reactions is discussed. This reaction class can be divided into three reaction categories: gas-to-solid (G2S), solid-to-gas (S2G), and solid-to-gas-to-gas (S2G2G). The established examples of G2S reactions are the gas-phase polymerizations of ethylene and propylene. However, other concepts, such as polymerization to butadiene rubber and synthesis of carbon nanotubes, are also discussed. It is a common feature of this reaction class that the catalyst remains a residue in the product and can influence its quality. S2G reactions are represented on a large scale by the synthesis of organosilanes. Another example is given by the hydrochlorination of silicon. In this reaction class, a particulate catalyst is anchored to the surface of the fluidized particles and should not be lost during the progressive conversion of the substrate. The fluidized-bed reactor is also suitable for performing the S2G2G reactions. Catalytic pyrolysis of biomass or waste is a good example of this class. In the first step, solid particles are thermally decomposed to gas and solid residue. 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Eng. Chem. Res</addtitle><date>2019-11-27</date><risdate>2019</risdate><volume>58</volume><issue>47</issue><spage>21173</spage><epage>21186</epage><pages>21173-21186</pages><issn>0888-5885</issn><eissn>1520-5045</eissn><abstract>In this review, the potential of fluidized-bed technology for heterogeneously catalyzed gas–solid reactions is discussed. This reaction class can be divided into three reaction categories: gas-to-solid (G2S), solid-to-gas (S2G), and solid-to-gas-to-gas (S2G2G). The established examples of G2S reactions are the gas-phase polymerizations of ethylene and propylene. However, other concepts, such as polymerization to butadiene rubber and synthesis of carbon nanotubes, are also discussed. It is a common feature of this reaction class that the catalyst remains a residue in the product and can influence its quality. S2G reactions are represented on a large scale by the synthesis of organosilanes. Another example is given by the hydrochlorination of silicon. In this reaction class, a particulate catalyst is anchored to the surface of the fluidized particles and should not be lost during the progressive conversion of the substrate. The fluidized-bed reactor is also suitable for performing the S2G2G reactions. Catalytic pyrolysis of biomass or waste is a good example of this class. In the first step, solid particles are thermally decomposed to gas and solid residue. In a consecutive step, gas released during pyrolysis is catalytically converted to value-added products.</abstract><pub>American Chemical Society</pub><doi>10.1021/acs.iecr.9b03515</doi><tpages>14</tpages><orcidid>https://orcid.org/0000-0002-9039-1310</orcidid></addata></record> |
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title | 110th Anniversary: Fluidized-Bed Chemical Reactors for Heterogeneously Catalyzed Gas–Solid Reactions: Old and New Applications |
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