Hydrogen Production by Steam Reforming of Pyrolysis Oil from Waste Plastic over 3 wt.% Ni/Ce-Zr-Mg/Al2O3 Catalyst

被引:3
|
作者
Han, Danbee [1 ]
Shin, Seungcheol [1 ]
Jung, Haneul [1 ]
Cho, Wonjun [2 ]
Baek, Youngsoon [1 ]
机构
[1] Univ Suwon, Dept Environm Energy Engn, 17 Wauan Gil, Hwaseong Si 18323, South Korea
[2] Bio Friends Inc, Daejeon 34028, South Korea
关键词
waste plastic; hydrogen; oil pyrolysis; Ni catalyst; steam reforming; BIOMASS TAR; RENEWABLE HYDROGEN; MODEL-COMPOUND; SUPPORTED NI; ACETIC-ACID; METHANE; CO; TOLUENE; SYNGAS; HYDROCARBONS;
D O I
10.3390/en16062656
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Sustained increase in plastic use has placed a significant burden on waste disposal infrastructure. Pyrolysis is the process of decomposing high-molecular-weight compounds by heating waste plastics at 500-1000 degrees C without oxygen. This process considerably reduces greenhouse gas emissions and has a high alternative energy effect (0.57 TOE ton(-1)). After a separation process, the oil produced by pyrolysis (C5-C20) can yield naphtha oil (C6-C7). Subsequently, hydrogen can be produced through a reforming reaction of this naphtha oil. Here, we produced hydrogen from waste plastic pyrolysis oil over a Ni/Ce-Zr-Mg/Al2O3 catalyst using a steam reforming process. A model oil combining the major substances of C6 and C7 (hexane, hexene, heptane, heptene, and toluene) was formed. From the reaction products, the hydrogen yield was obtained based on analysis of H-2, CO, and CO2 concentrations using gas chromatography. The effect of N-2 and O-2 addition on hydrogen yield was analyzed within a temperature range of 750-850 degrees C, steam/carbon (S/C) ratio of 0.6-4, and space velocity of 7600-19,100 h(-1). In addition, a durability test was performed using 3 wt.% Ni/Ce-Zr-Mg/Al2O3 catalysts for 100 h; a hydrogen yield of 91.3% was maintained from the refined waste plastic oil.
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页数:14
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