Plastic Waste and Recycling 2020
DOI: 10.1016/b978-0-12-817880-5.00012-8
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Blast furnace feedstock and coke oven chemical feedstock

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Cited by 3 publications
(4 citation statements)
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“…The kinetics of thermal degradation and the activation energy of PEs during TGA measurements in an argon environment have been reported, and equations have been presented to assess the phenomena occurring in polymeric materials during thermal degradation [106][107][108][109]. Additionally, solid carbon residue is not formed despite an inert atmosphere, which is a common behavior of Pes, as reported in the literature [110]. The behavior of HDPE at 250-300 • C, at the beginning of HDPE degradation, is a common behavior of HDPE in TGA measurements, as presented in the literature [111,112].…”
Section: Tga and Dsc Analysis Resultsmentioning
confidence: 99%
“…The kinetics of thermal degradation and the activation energy of PEs during TGA measurements in an argon environment have been reported, and equations have been presented to assess the phenomena occurring in polymeric materials during thermal degradation [106][107][108][109]. Additionally, solid carbon residue is not formed despite an inert atmosphere, which is a common behavior of Pes, as reported in the literature [110]. The behavior of HDPE at 250-300 • C, at the beginning of HDPE degradation, is a common behavior of HDPE in TGA measurements, as presented in the literature [111,112].…”
Section: Tga and Dsc Analysis Resultsmentioning
confidence: 99%
“…) due to dissociation, sensible heat, reverse water-gas shift of the H 2 , incomplete combustion with the O 2 , and transfer of S to the slag, kcal/mol j q k heat absorbed at T R by the total H 2 in the furnace when considering that it is completely converted to H 2 O through the reverse water-gas shift reaction, kcal/mol H2 q mid energy consumption to heat the shaft injection to T R , kcal/ mol mid q Mn heat absorbed at T R by the reaction C + MnO→CO + Mn, kcal/mol O q P heat absorbed at T R by the reaction1/5P number of moles of CO produced via the direct reduction of Non-steel sectors, such as plastic consumers, are also an important sources of syngas for iron-making (in this case, the syngas would not be CO 2 -neutral). As occurred in the case of biomass, the utilization of waste plastic in ironmaking has been usually proposed in literature as a pulverized solid fuel injection [19][20][21], instead of as syngas injection. Nevertheless, waste plastic can be gasified to generate syngas and partially substitute coke and pulverized coal.…”
Section: Introductionmentioning
confidence: 99%
“…(b) Chemical or feedstock recycling (Bauer and Lehner, 2013; Garforth et al, 2004; Ignatyev et al, 2014; Nomura, 2020; Pohjakallio and Vuorinen, 2020; Ragaert et al, 2017; Soto et al, 2018): this type of recycling has a high potential for heterogeneous and contaminated plastic waste material if more intensive separation and processing than in case of mechanical recycling is neither economically nor technically feasible. A dry-mechanical pre-treatment of input materials is also necessary for chemical recycling.…”
Section: Introductionmentioning
confidence: 99%
“…Other important processes are pyrolysis, hydrogenation, gasification, and substitute reducing agents in the blast furnace process. The strict quality requirements for the input material are shown in Table 1, for example, for thermochemical conversion (ReOil-process) (Lechleitner et al, 2019) and the use as a reducing agent in the blast furnace process (Nomura, 2020).…”
Section: Introductionmentioning
confidence: 99%