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Aromatic Light Hydrocarbon Fuel Generation from Municipal Polystyrene (PS) Waste Plastic by Using Low Temperature Fractional Distillation Process

机译:低温分馏工艺从市政聚苯乙烯(PS)废塑料中生产芳香族轻烃燃料

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Everyday the use of plastic is increasing because plastic has light weight and durability. After use, all plastics are thrown into garbage station because some plastic are one-off and creating plastic garbage. Worldwide PS waste plastic is generating 9-10%. Polystyrene plastic formula is C8H8 and this plastic has benzene compound. Thermal degradation processes PS waste plastic breakdown long chain to short chain hydrocarbon without using any kind of catalyst. Polystyrene waste plastic to light fractional fuel production processes was two steps process. 1st step process temperature range was 100-400 ºC for polystyrene waste plastic to polystyrene fuel production. 2nd step process was polystyrene fuel into light fractional aromatic hydrocarbon fuel production processes and temperature range was 40-60 ºC. Light fractional aromatic hydrocarbon fuel separation done by fractional distillation column process. 1st step PS waste plastic to liquid fuel density is 0.88 gm/ml and 2nd step light fractional liquid fuel density is 0. 84 gm/ml. Produced fuel was analyzed by Gas Chromatography and Mass Spectrometer, Fourier Transform Infrared Spectrometer and Differential Scanning Calorimeter to determine liquid fuel compound structure, fuel band energy and fuel boiling point.
机译:由于塑料重量轻且经久耐用,因此塑料的使用量每天都在增加。使用后,所有塑料都被扔进垃圾站,因为有些塑料会一次性丢弃并产生塑料垃圾。全球PS废塑料占9-10%。聚苯乙烯塑料分子式为C8H8,该塑料具有苯化合物。热降解工艺不使用任何催化剂就可将PS废塑料从长链降解为短链烃。聚苯乙烯废塑料到轻质分馏燃料的生产过程分为两步过程。对于聚苯乙烯废塑料到聚苯乙烯燃料的生产,第一步温度范围为100-400ºC。第二步工艺是将聚苯乙烯燃料转化为轻质芳烃燃料分馏工艺,温度范围为40-60ºC。通过分馏塔工艺完成轻质芳烃燃料分离。第一步PS废塑料对液体燃料的密度为0.88 gm / ml,第二步轻质液体燃料的分数为0. 84 gm / ml。用气相色谱和质谱仪,傅立叶变换红外光谱仪和差示扫描量热仪分析产生的燃料,以确定液体燃料化合物的结构,燃料带能和燃料沸点。

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