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Co-pyrolysis of Fe_3O_4-poly(vinyl chloride) (PVC) mixtures: Mitigation of chlorine emissions during PVC recycling

机译:Fe_3O_4-聚(氯乙烯)(PVC)混合物的共热分解:PVC回收过程中氯排放的减轻

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A systematic investigation was conducted on the co-pyrolysis of Fe_3O_4 and PVC mixtures in temperatures as high as 1373 K upon the development of PVC recycling technology that mitigates chlorine emission. Central to our investigation, PVC decomposition plays the leading role in the co-pyrolysis of Fe_3O_4 and PVC mixtures following a two-stage pattern bifurcated at a temperature of 673 K. In Stage 1, at temperatures 673 K and lower, Fe_3O_4 is chlorinated by chlorine from PVC, resulting in FeCl_2. The composition of the final solid residue of Stage 1, conjugated polyene, FeCl_2 and Fe_3O_4/Fe_2O_3, depends on the initial Fe_3O_4 content in the mixture. When the temperature is increased to be higher than 673 K, decomposition of conjugated polyene occurs simultaneously with the stepwise reduction of Fe_3O_4/Fe_2O_3: Fe_2O_3 → Fe_3O_4→ FeO → Fe. However, in mixtures containing Fe_3O_4 that is less than 39.6% of the mass, Fe_3O_4 can coexist with Fe; therefore, the FeO formation step is skipped. Most FeCl_2 escapes from the reaction system as vapor, showing the necessity of removing FeCl_2 at the end of Stage 1 to avoid harmful substance emission. The presence of Fe_3O_4 can significantly suppress gaseous emissions, especially HC1 originating from PVC decomposition. There was only 0.6% HC1 by mass (2.4% PVC base by mass) released when co-pyrolyzing the PVC + 75% Fe_3O_4 mixture due to the complete consumption of PVC and its decomposition products by Fe_3O_4. After separating FeCl_2, which is a valuable chemical feedstock, by water-leaching the solid residue obtained at 673 K, the filtered residue, which is a mixture of Fe_3O_4/ Fe_2O_3 and polyene, was confirmed to be suitable for iron-making. The results clearly show the possibility of developing a PVC recycling technology with mitigated chlorine emissions by manipulating the amount of Fe_3O_4 added.
机译:在PVC回收技术的开发后,在高达1373K的温度下的Fe_3O_4和PVC混合物的共热解中进行了系统的研究,减轻了氯发射的PVC回收技术。我们的研究中的核心,PVC分解在Fe_3O_4和PVC混合物的共热解中起到在673K温度的两级图案之后的Fe_3O_4和PVC混合物中的主要作用。在第1阶段,在673k和更低的温度下,Fe_3O_4被氯化来自PVC的氯,导致FECL_2。第1阶段1,缀合的多烯,FECL_2和Fe_3O_4 / Fe_2O_3的最终固体残余物的组成取决于混合物中的初始Fe_3O_4含量。当温度升高至高于673k时,共轭多烯的分解同时发生Fe_3O_4 / Fe_2O_3:Fe_2O_3→Fe_3O_4→Feo→Fe。然而,在含有少于39.6%的Fe_3O_4的混合物中,Fe_3O_4可以与Fe共存;因此,跳过了Feo形成步骤。大多数FECL_2从反应系统中逸出为蒸气,显示在第1阶段结束时去除FECL_2以避免有害物质排放。 Fe_3O_4的存在可以显着抑制气态排放,尤其是源自PVC分解的HC1。由于FE_3O_4的完全消耗,仅在PVC + 75%FE_3O_4混合物中释放出PVC + 75%FE_3O_4混合物时,只有0.6%HC1质量(2.4%PVC基础)释放。在分离FECL_2之后,通过水浸出在673k中获得的固体残余物,确认是Fe_3O_4 / Fe_2O_3和聚烯的混合物的过滤的残余物适用于铁制剂。结果清楚地表明,通过操纵加入的Fe_3O_4的量,通过操纵氯排放的PVC再循环技术的可能性。

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