Application of fuel reforming in waste heat recovery technologies for combustion systems

被引:0
|
作者
Sun Z. [1 ]
Gu G. [2 ]
Zhou C. [1 ]
Guo Q. [1 ]
Lan J. [2 ]
Lyu T. [2 ]
Han D. [1 ]
机构
[1] Key Laboratory for Power Machinery and Engineering, Ministry of Education, Shanghai Jiao Tong University, Shanghai
[2] Shanghai Marine Diesel Engine Research Institute, Shanghai
关键词
auto-thermal reforming; catalysts; chemical recuperation; combustion burner; combustion engine; dry reforming; gas turbine; steam reforming;
D O I
10.11990/jheu.202202019
中图分类号
学科分类号
摘要
Basing on the state of art for the application of reforming technology on waste heat recovery, progress in reforming mechanisms, heat recovery systems, and the designs of fuel reformer is reviewed. From previous works, different reforming methods show the varied reaction temperatures and carbon deposition characteristics due to the deviation in their total enthalpy change and the products. Fuel reforming studies on internal combustion engine, gas turbine, and combustion boiler indicate that fuel reforming contributes to thermal efficiency improvement and emissions reduction. The reformer design with mixing followed by heat exchange is beneficial for mixture uniformity improvement, but this tends to cause coking in the reactor, and vice versa. Noble metal catalysts can significantly suppress the carbon deposition in the reactor. © 2023 Editorial Board of Journal of Harbin Engineering. All rights reserved.
引用
收藏
页码:257 / 267
页数:10
相关论文
共 49 条
  • [1] ZHANG Zunhua, JIA Pengpeng, ZHONG Geyu, Et al., Numerical study of exhaust reforming characteristics on hydrogen production for a marine engine fueled with LNG, Applied thermal engineering, 124, pp. 241-249, (2017)
  • [2] ZHANG Zunhua, WU Renmin, FENG Shangsheng, Et al., Numerical investigation of tubular exhaust reformer with thermochemical recuperation for LNG engine, International journal of heat and mass transfer, 146, (2020)
  • [3] PACHECO M, SIRA J, KOPASZ J., Reaction kinetics and reactor modeling for fuel processing of liquid hydrocarbons to produce hydrogen: isooctane reforming, Applied catalysis A: general, 250, 1, pp. 161-175, (2003)
  • [4] LIU Shuyuan, FENG Yu, CHU Yuchuan, Et al., Numerical study of catalytic steam reforming of aviation kerosene at supercritical pressures, Fuel, 212, pp. 375-386, (2018)
  • [5] CREASER D, KARATZAS X, LUNDBERG B, Et al., Modeling study of 5 kWe-scale autothermal diesel fuel reformer, Applied catalysis A: general, 404, 1, pp. 129-140, (2011)
  • [6] ZAZHIGALOV S V, SHILOV V A, ROGOZHNIKOV V N, Et al., Modeling of hydrogen production by diesel reforming over Rh/ Ce<sub>0. 75</sub>Zr<sub>0. 25</sub>O<sub>2</sub>-δ-η-Al<sub>2</sub>O<sub>3</sub> / FeCrAl wire mesh honeycomb catalytic module, Catalysis today, 378, pp. 240-248, (2021)
  • [7] CHEN W H, CHEN C Y., Water gas shift reaction for hydrogen production and carbon dioxide capture: a review, Applied energy, 258, (2020)
  • [8] ECKLE S, ANFANG H G, BEHM R J., Reaction intermediates and side products in the methanation of CO and CO<sub>2</sub> over supported Ru catalysts in H<sub>2</sub>-rich reformate gases, The journal of physical chemistry C, 115, 4, pp. 1361-1367, (2011)
  • [9] BURCH R., Gold catalysts for pure hydrogen production in the water-gas shift reaction: activity, structure and reaction mechanism, Physical chemistry chemical physics: PC-CP, 8, 47, pp. 5483-5500, (2006)
  • [10] DE LIMA S M, DA SILVA A M, DA COSTA L O O, Et al., Study of catalyst deactivation and reaction mechanism of steam reforming, partial oxidation, and oxidative steam reforming of ethanol over Co/ CeO<sub>2</sub> catalyst, Journal of catalysis, 268, 2, pp. 268-281, (2009)