Hydrogen Production from Glycerol and Plastics by Sorption-Enhanced Steam Reforming

被引:0
|
作者
Chunakiat, Petch [1 ]
Panarmasar, Nipitpon [2 ]
Kuchonthara, Prapan [1 ,3 ,4 ]
机构
[1] Chulalongkorn Univ, Fac Sci, Fuels Res Ctr, Dept Chem Technol, Bangkok 10330, Thailand
[2] Chulalongkorn Univ, Fac Sci, Program Petrochem & Polymer Sci, Bangkok 10330, Thailand
[3] Chulalongkorn Univ, Ctr Excellence Catalysis Bioenergy & Renewable Che, Phayathai Rd, Bangkok 10330, Thailand
[4] Ctr Excellence Petrochem & Mat Technol PETROMAT, Bangkok 10330, Thailand
关键词
CRUDE GLYCEROL; CALCIUM-OXIDE; CO-PYROLYSIS; BIOMASS; GASIFICATION; CATALYSTS; ETHANOL; GAS; BED; CHAR;
D O I
10.1021/acs.iecr.3c02072
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hydrogen (H-2) serves as a vital precursor in numerous processes, and it is envisioned to serve as a clean energy source in the future. The utilization of waste materials for the production of H-2 presents a noteworthy opportunity to advance the sustainability of H-2-based energy. In this study, the effect of cofeeding three different types of plastic, polyethylene (PE), polypropylene (PP), and polystyrene (PS), with glycerol was investigated in the two-step process of pyrolysis and steam reforming (PSR) to produce H-2. Experiments were performed using a two-stage fixed bed reactor at 973 K. For each type of plastic, the yield of H-2 in the copresence of glycerol was higher than the combined yield of that from the plastic and glycerol separately. This result demonstrated the effectiveness of the synergistic relationship between plastics and glycerol in enhancing H-2 production through PSR. Among the plastics, PE gave the highest H-2 yield followed by PP and PS. Bifunctional nickel oxide/calcium oxide (NiO-CaO) catalysts were synthesized for the pyrolysis sorption-enhanced steam reforming process (PSESR) of plastics with glycerol at 973 K. The maximum H-2 yield was obtained from the PSESR of PE with glycerol when using a NiCa/silica fiber (SF) catalyst. Using NiO combined with CaO in PSESR can promote the cracking of volatile pyrolysis products, reducing the coke deposition and increasing CO2 adsorption. Furthermore, the nonporous structure of the SF support afforded easier access to the active sites in comparison to the conventional porous alumina support.
引用
收藏
页码:21057 / 21066
页数:10
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