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  • 教师姓名: 徐东海
  • 职称: 教授
  • 职务: 国家级青年人才、能动学院热能工程系主任、西安市先进生物质能技术国际科技合作基地主任
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Catalyzed Partial Oxidative Gasification of Phenol in Supercritical Water

发布时间:2025-04-30
点击次数:
发布时间:
2025-04-30
论文名称:
Catalyzed Partial Oxidative Gasification of Phenol in Supercritical Water
发表刊物:
Industrial & Engineering Chemistry Research
摘要:
Phenol, a substance difficult to be gasified, is often an intermediate product from biomass gasification in supercritical water. In this study, 1 wt % phenol is gasified in supercritical water with different oxidation coefficients (0 ≤ n ≤ 0.8) at 430−550 °C, 25 MPa in a continuous tubular-flow reaction plant with or without 0.1 wt % Na2CO3. The results show that TOC (total organic carbon) removal rate and COD (chemical oxygen demand) removal rate of reactor effluent will rise with the increase of oxidation coefficient and reaction temperature. When n rises from 0.3 to 0.8 at 500 °C, hydrogen yield and hydrogen molar fraction will first increase and then decrease. They reach their respective maximum values of 0.245 mol/mol and 46.2% at n = 0.6 with the residence time of 2.96 min. There is an appropriate oxidation coefficient for obtaining the highest hydrogen yield for phenol supercritical water partial oxidative gasification (SWPO). Na2CO3 can serve as a catalyst or an additive for phenol SWPO. When 0.1 wt % Na2CO3 is added, hydrogen yield is near 0.477 mol/mol at n = 0.6, 500 °C with the residence time of 2.96 min. Furthermore, the potential conversion pathways for phenol SWPO with Na2CO3 catalyst are also proposed.
合写作者:
Donghai Xu, Shuzhong Wang, Yang Guo, Xingying Tang, Yanmeng Gong, Honghe Ma
卷号:
2011, 50(8)
页面范围:
4301-4307
是否译文:
否
发表时间:
2011-03-15