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Catalytic and thermal oxidative pyrolysis of LDPE in a continuous reactor system

机译:连续反应器系统中LDPE的催化和热氧化热解

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In this work, low-density polyethylene (LDPE) plastic which is a mager product within plastics and formed a high amount of waste was chosen as a material to be worked. LDPE was both decomposed thermally and catalytic in a continuous reactor via as an oxidative media. Catalytic and thermal processes were investigated at the temperature range of 400-500℃ and raw material feeding at a rate of 0.7 g min~(-1). As a result of degradation, the maximum liquid yield, acid and peroxid numbers of liquid products in thermal and catalytic oxidative media at 400℃ temperature and 600 mL min~(-1) air flow rate conditions have determined as 102%, 28, 52 and 75%, 16 and 43, respectively. In addition, the molecular weight of liquid products were determined by GC/MS system and found that oxygenic compounds for thermal and catalytic oxidative pyrolysis aproximately 50 and 27%, respectively.
机译:在这项工作中,选择低密度聚乙烯(LDPE)塑料作为工作材料,该材料是塑料中的较大产品,并且形成大量废物。 LDPE在连续反应器中通过氧化介质热分解和催化分解。研究了在400-500℃温度范围内的催化和热过程,原料进料速率为0.7 g min〜(-1)。作为降解的结果,在400℃温度和600 mL min〜(-1)空气流量条件下,热和催化氧化介质中液体产物的最大液体收率,酸和过氧化物数已确定为102%,28、52和75%,16和43。另外,通过GC / MS系统测定液体产物的分子量,发现用于热和催化氧化热解的含氧化合物分别约50%和27%。

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