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首页> 外文期刊>Science and Technology Indonesia >Polystyrene Plastic Waste Conversion into Liquid Fuel with Catalytic Cracking Process Using Al2O3 as Catalyst
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Polystyrene Plastic Waste Conversion into Liquid Fuel with Catalytic Cracking Process Using Al2O3 as Catalyst

机译:Al2O3催化裂化工艺将聚苯乙烯塑料废料转化为液体燃料

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The increase in energy consumption and an increase in the plastic waste generation are two major problems that arise along with economic growth and the increase in population. Styrofoam is one type of polystyrene plastic waste that can be processed into liquid fuels by cracking process. In this study, the cracking process of polystyrene plastic waste into liquid fuel carried by the catalytic cracking process using Al2O3 as a catalyst. This study aimed to determine the effect of the catalyst weight, length of cracking time and range of temperature in the catalytic cracking process of polystyrene plastic waste into liquid fuel toward the mass and characteristics of liquid fuels produced and to determine the composition of liquid fuels produced. The catalytic cracking process of polystyrene plastic waste with catalyst was done in the fixed bed type reactor by heating the reactor with a heater, where the process took place at temperature of 150°C, 200°C, 250°C and 300°C and the length of the process was varied into 20, 40, and 60 minutes and the catalyst weight was also varied, which were 4%, 6% and 8%, while the styrofoam weight was 250 grams. From the research, the highest mass of liquid fuel derived from polystyrene catalytic cracking process was in the amount of 48.8 grams and liquid yield percentage of 19.5% at temperature of 250°C, cracking time of 60 minutes and weight of 8% catalyst, while the characteristics of liquid fuel that were approaching the characteristics of gasoline was at temperatures of 250°C, cracking time of 60 minutes and weight of 6% catalyst, in which each value of density of 0.763 g/ml, specific gravity of 0.778 and oAPI gravity of 50.2. While other liquid fuels obtained from the cracking of polystyrene were still within the tolerance range characteristic properties of gasoline. Liquid fuels produced from the catalytic cracking process was analyzed using a GC-MS, in which the analysis results indicated that liquid fuels were included in the gasoline fraction.
机译:能源消耗的增加和塑料废物产生的增加是伴随经济增长和人口增加而出现的两个主要问题。聚苯乙烯泡沫塑料是一种聚苯乙烯塑料废料,可以通过裂化工艺将其加工成液体燃料。在这项研究中,采用Al2O3作为催化剂的催化裂化工艺将聚苯乙烯塑料废料裂解为液体燃料。这项研究旨在确定催化剂重量,裂化时间长度和温度范围在聚苯乙烯塑料废料催化裂化过程中对液体燃料的质量和特性的影响,并确定所生产的液体燃料的组成。聚苯乙烯塑料废料与催化剂的催化裂化过程是在固定床式反应器中通过用加热器加热反应器完成的,该过程在150°C,200°C,250°C和300°C的温度下进行,该过程的长度被改变为20、40和60分钟,催化剂的重量也被改变,分别为4%,6%和8%,而泡沫聚苯乙烯的重量为250克。根据研究,在250°C的温度,60分钟的裂解时间和8%的催化剂重量下,聚苯乙烯催化裂化工艺得到的最高液体燃料质量为48.8克,液体产率为19.5%。接近汽油特性的液体燃料特性是在250°C的温度,60分钟的裂解时间和6%的催化剂重量下进行的,其中每个密度值为0.763 g / ml,比重为0.778和oAPI重力为50.2。虽然从聚苯乙烯裂解获得的其他液体燃料仍在汽油的特性范围内。使用GC-MS对催化裂化过程产生的液体燃料进行了分析,分析结果表明,汽油馏分中包含液体燃料。

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