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Catalytic Thermal Cracking of Postconsumer Waste Plastics to Fuels. 2. Pilot-Scale Thermochemical Conversion

机译:消费后废塑料催化转化为燃料的热裂解。 2.中试热化学转化

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摘要

Synthetic gasoline and diesel fuels were prepared via catalytic and noncatalytic pyrolysis of waste polyethylene and polypropylene plastics followed by distillation of plastic crude oils. Reaction conditions optimized using a 2 L batch reactor were applied to pilot-scale production of plastic crude oil from polypropylene. The optimum conditions on the pilot-scale system were a reaction temperature of 500 degrees C and a residence time of 4.7 min. Plastic crude oil yields at pilot scale were comparable to those of the batch scale (70-80%). Plastic crude oils obtained from pyrolysis were distilled into the boiling point range of motor gasoline, diesel no. 1, gas oil, and vacuum gas oil range fractions. The elemental composition of the crude oil and its distillates were similar to the starting plastic material. Fuel properties were studied for both neat and in blends (5% and 20%) with ultralow sulfur diesel fuel (ULSD). Excellent low temperature properties were obtained for some of the samples, as indicated by a pour point of <-74 degrees C and cold filter plugging point (CFPP) of <-50 degrees C. Oxidative stabilities and kinematic viscosities of plastic diesel-range samples were found to be within the limits prescribed in American (ASTM D975) and European (EN 590) petroleum standards, where applicable. In addition, the plastic diesel-range samples yielded greater energy content than ULSD. Three plastic diesel-range samples were selected for further evaluation as blend components in ULSD, as these were determined to have the best combination of fuel properties relative to the other diesel-range samples. The 5 and 20% blends exhibited superior low temperature performance relative to ULSD. In addition, oxidative stability was not negatively affected by blend ratio. All blends provided oxidative stabilities and kinematic viscosities within the ranges specified in the petrodiesel standards. Density decreased slightly and energy content increased with increasing concentration of the plastic diesel-range sample in ULSD. In summary, our results demonstrated that a plastic diesel-range sample prepared from pilot-scale pyrolysis of waste plastics followed by distillation can be used as drop-in or as blend components with ULSD without negatively affecting fuel properties of ULSD.
机译:合成汽油和柴油燃料是通过废旧聚乙烯和聚丙烯塑料的催化和非催化热解,然后蒸馏塑料原油而制备的。将使用2 L分批反应器优化的反应条件应用于从聚丙烯中试规模生产塑料原油。中试规模系统的最佳条件是反应温度为500摄氏度,停留时间为4.7分钟。中试规模的塑料原油收率可与批量生产的比例相媲美(70-80%)。将通过热解获得的塑料原油蒸馏到汽车汽油(编号1)的沸点范围内。 1,粗柴油和真空粗柴油的馏分。原油及其馏出物的元素组成与起始塑料相似。研究了与超低硫柴油(ULSD)混合的混合燃料(5%和20%)的燃料性能。某些样品获得了优异的低温性能,如倾点<-74摄氏度和冷滤器堵塞点(CFPP)≤-50摄氏度。塑料柴油系列样品的氧化稳定性和运动粘度被发现在适用的美国(ASTM D975)和欧洲(EN 590)石油标准规定的范围内。此外,塑料柴油系列样品产生的能量含量高于ULSD。选择了三个塑料柴油系列样品作为ULSD中的混合组分进行进一步评估,因为相对于其他柴油系列样品,它们被确定具有最佳的燃料特性组合。相对于ULSD,5%和20%的混合物表现出优异的低温性能。另外,混合比例对氧化稳定性没有负面影响。所有掺混物的氧化稳定性和运动粘度均在石油柴油标准规定的范围内。随着ULSD中塑料柴油系列样品浓度的增加,密度略有下降,能量含量增加。总而言之,我们的结果表明,由废塑料的中试规模热解然后蒸馏制得的塑料柴油系列样品可以用作ULSD的直接入料或掺混组分,而不会负面影响ULSD的燃料性能。

著录项

  • 来源
    《Energy & fuels》 |2017年第3期|2705-2715|共11页
  • 作者单位

    Univ Illinois, Prairie Res Inst, Illinois Sustainable Technol Ctr, Urbana, IL 61820 USA;

    Univ Illinois, Prairie Res Inst, Illinois Sustainable Technol Ctr, Urbana, IL 61820 USA;

    ARS, Biooils Res Unit, Natl Ctr Agr Utilizat Res, USDA, Peoria, IL 61604 USA;

    Univ Illinois, Prairie Res Inst, Illinois Sustainable Technol Ctr, Urbana, IL 61820 USA;

    Univ Tennessee, Ctr Renewable Carbon, 2506 Jacob Dr, Knoxville, TN 37996 USA;

    Univ Illinois, Prairie Res Inst, Illinois Sustainable Technol Ctr, Urbana, IL 61820 USA;

    Univ Illinois, Prairie Res Inst, Illinois Sustainable Technol Ctr, Urbana, IL 61820 USA;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
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