A mathematical model and numerical investigation for glycerol gasification in supercritical water with a tubular reactor

被引:50
|
作者
Jin, Hui [1 ]
Guo, Simao [1 ]
Guo, Liejin [1 ,2 ]
Cao, Changqing [1 ]
机构
[1] Xi An Jiao Tong Univ, State Key Lab Multiphase Flow Power Engn, Xian 710049, Peoples R China
[2] King Abdulaziz Univ, Dept Mech Thermal Engn & Chem & Mat Engn, Coll Engn, Jeddah 21589, Saudi Arabia
来源
基金
中国国家自然科学基金;
关键词
Supercritical water gasification; Tubular reactor; Numerical study; Glycerol; Hydrogen production; HYDROGEN-PRODUCTION; BIOMASS GASIFICATION; HEAT-TRANSFER; COAL-GASIFICATION; GLUCOSE; OXIDATION; HYDROPYROLYSIS; CONVERSION; FEEDSTOCK; LIGNIN;
D O I
10.1016/j.supflu.2015.06.028
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
This paper developed a three-dimensional computational fluid dynamics model of the supercritical water gasification (SCWG) process of glycerol. The detailed flow field, temperature field and chemical species distributions inside the reactor were revealed, and the effects of the operating parameters on the results in the SCWG of glycerol were investigated. The reasons for incomplete gasification were discussed, and relevant possible improvements were proposed. (1) The residence time is not long enough for the complete gasification; therefore, the optimal length of the tubular reactor was obtained under different operating conditions. (2) A side-reaction region was formed near the feeding inlet and methods to reduce the volume of the side-reaction region were investigated. A high preheated water temperature and a 135 degrees feeding angle were proved to obviously avoid side-reaction. A multi-injection feeding method can also suppress the side-reaction, but the carbon gasification efficiency decreased. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:526 / 533
页数:8
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