化学
除氧
选择性
催化作用
热解
碳氢化合物
吸附
脱羧
无机化学
核化学
有机化学
作者
Shogo Kumagai,Ryota Yamasaki,Tomohito Kameda,Yuko Saito,Atsushi Watanabe,Chuichi Watanabe,Norio Teramae,Toshiaki Yoshioka
标识
DOI:10.1016/j.cej.2017.09.077
摘要
During the tandem pyrolysis of poly(ethylene terephthalate) (PET) and catalytic conversion of the PET pyrolysates over calcium oxide (PET/CaO process), the relationship between catalyst deterioration and the aromatic hydrocarbon selectivity was elucidated. Using a tandem micro (µ)-reactor-gas chromatography/mass spectrometry (TR-GC/MS) system, PET was pyrolyzed at 450 °C in the 1st µ-reactor and the PET pyrolysates were refined over one of two CaO catalysts with different basicities at 700 °C in the 2nd µ-reactor. Strongly basic CaO enhanced benzene production via decarboxylation, resulting in 83.6% selectivity for aromatic hydrocarbon products. This selectivity decreased with repeated runs over the strongly basic CaO, while oxygen-containing compounds such as benzophenone and benzoic acid increased. The surface morphology changes observed by scanning electron microscopy indicated that CaO was thoroughly sintered with repeated use, which reduced its basicity. The less-basic CaO effected diminished carboxyl-unit surface adsorption and suffered deteriorated deoxygenation ability. Thus, this study clearly demonstrates that CaO deterioration (by sintering during repeated PET/CaO processing) and CaO basicity strongly influence reaction selectivity.
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