共 38 条
Hydrogen production by partial oxidation gasification of a phenol, naphthalene, and acetic acid mixture in supercritical water
被引:45
作者:
Wang, Yuzhen
[1
,2
]
Wang, Shuzhong
[2
]
Zhao, Gaoyang
[1
]
Guo, Yanfeng
[1
]
Guo, Yang
[2
]
机构:
[1] Xian Univ Technol, Xian 710048, Shaanxi, Peoples R China
[2] Xi An Jiao Tong Univ, Key Lab Thermofluid Sci & Engn MOE, Xian 710049, Peoples R China
基金:
中国博士后科学基金;
关键词:
Supercritical water partial oxidation;
Hydrogen;
Phenol;
Naphthalene;
Acetic acid;
REACTION PATHWAYS;
BIOMASS GASIFICATION;
REACTION-KINETICS;
N-HEXADECANE;
MODEL;
LIGNIN;
NAOH;
CONVERSION;
GLYCEROL;
GLUCOSE;
D O I:
10.1016/j.ijhydene.2015.12.115
中图分类号:
O64 [物理化学(理论化学)、化学物理学];
学科分类号:
070304 ;
081704 ;
摘要:
A mixture of phenol, acetic acid, and naphthalene was partially oxidized in supercritical water in order to produce hydrogen. The effects of temperature, oxidation ratio (OR), reaction time, and reactant concentrations on gaseous distributions, gasification efficiencies, and reactants removal efficiencies were investigated. Furthermore, the effects of oxygen on the main intermediate products were analyzed, and possible degradation pathways were proposed. Results indicated that higher temperatures significantly promoted the H-2 yield. In addition, small amounts of oxygen (OR <0.2) accelerated the production of H-2 and CH4. The maximum H-2 gasification efficiency (240.25%) and H-2 yield (70.16 mmol g(-1)) were obtained at 560 degrees C, 25 MPa, reaction time of 20 s and OR of 0.2. Longer reaction time enhanced the gasification efficiencies in 10 s, while the effect was little when reaction times longer than 10 s. The concentrations of the reactants did not significantly influence the gasification efficiencies. Copyright (C) 2015, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:2238 / 2246
页数:9
相关论文