Entrained Flow Gasification of Polypropylene Pyrolysis Oil

被引:19
作者
Weiland, Fredrik [1 ]
Qureshi, Muhammad Saad [2 ]
Wennebro, Jonas [1 ]
Lindfors, Christian [2 ]
Ohra-aho, Taina [2 ]
Shafaghat, Hoda [1 ]
Johansson, Ann-Christine [1 ]
机构
[1] RISE Energy Technol Ctr AB, Box 726, SE-94128 Pitea, Sweden
[2] VTT Tech Res Ctr Finland Ltd, POB 1000, FI-02044 Espoo, Finland
关键词
pyrolysis; gasification; syngas; chemical recycling; plastic waste; HIGH-DENSITY POLYETHYLENE; FLUIDIZED-BED REACTOR; BLACK LIQUOR; PLASTIC WASTE; BIOMASS GASIFICATION; CATALYTIC PYROLYSIS; CO-GASIFICATION; TEMPERATURE; YIELD; FUEL;
D O I
10.3390/molecules26237317
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
Petrochemical products could be produced from circular feedstock, such as waste plastics. Most plants that utilize syngas in their production are today equipped with entrained flow gasifiers, as this type of gasifier generates the highest syngas quality. However, feeding of circular feedstocks to an entrained flow gasifier can be problematic. Therefore, in this work, a two-step process was studied, in which polypropylene was pre-treated by pyrolysis to produce a liquid intermediate that was easily fed to the gasifier. The products from both pyrolysis and gasification were thoroughly characterized. Moreover, the product yields from the individual steps, as well as from the entire process chain, are reported. It was estimated that the yields of CO and H-2 from the two-step process were at least 0.95 and 0.06 kg per kg of polypropylene, respectively, assuming that the pyrolysis liquid and wax can be combined as feedstock to an entrained flow gasifier. On an energy basis, the energy content of CO and H-2 in the produced syngas corresponded to approximately 40% of the energy content of the polypropylene raw material. This is, however, expected to be significantly improved on a larger scale where losses are proportionally smaller.
引用
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页数:16
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