4.7 Article

Processing of low-density waste in fluidized bed made out of lightweight expanded clay aggregate

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JOURNAL OF CLEANER PRODUCTION
卷 349, 期 -, 页码 -

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ELSEVIER SCI LTD
DOI: 10.1016/j.jclepro.2022.131328

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Fluidized-bed combustion; Lightweight expanded clay aggregate; Polyolefins; Glycerol

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The aim of this study is to develop a new method for combustion processes in fluidized bed reactors. The use of a fluidized bed made out of lightweight expanded clay aggregate (LECA) has shown promising results for thermal processing of low-density solid and liquid industrial wastes, as well as waste biomass. The experiments conducted in the LECA fluidized bed demonstrated high conversion rates of carbon, with over 95% conversion achieved for polyolefins. Waste wood chips were successfully incinerated as alternative fuel in the LECA fluidized bed.
The main aim of the study is to obtain a new, innovative method for the organization of combustion processes in fluidized bed reactors. A key aspect of the change in the organization of the fluidized bed combustion process is the creation of a fluidized bed made out of lightweight expanded clay aggregate (LECA). The new fluidized bed has a density of 0.5 g/cm(3), therefore, allowing for thermal processing of low-density solid and liquid industrial wastes, as well as waste biomass. Polyolefins (polyethylene, linear low-density polyethylene, high-density polyethylene, polypropylene, and polypropylene homopolymer) were selected as examples of low-density solid wastes. The use of an innovative fluidized bed for liquid waste degradation was studied on the example of glycerol combustion. Waste wood chips were chosen to represent low-density biomass. Thermal degradation of selected materials in the fluidized bed made out of LECA was carried out at a temperature range of 500-900 degrees C with an interval of 100 degrees C. Video analysis of the fluidized bed surface proved the sinking of waste materials into the bed and significant elimination of diffusion flames in the freeboard. Qualitative and quantitative flue gas analysis was carried out using the FTIR spectrometer. More than 95% conversion of the carbon contained in the polyolefins to CO2 was achieved already at 700 degrees C. At 500 degrees C, more than 30% of the polymeric carbon left the reactor as aromatic compounds. To avoid the emission of harmful aldehydes during the thermal processing of glycerol, the bed should be heated to at least 800 degrees C. Waste wood chips as an alternative fuel can be thermally incinerated in the fluidized bed made out of LECA. The disappearance of volatile organic compounds and CO emissions occurred at 700 degrees C and 800 degrees C.

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