Modeling the Thermal De-NOx Process:: Closing in on a final solution

被引:2
|
作者
Miller, JA [1 ]
Glarborg, P
机构
[1] Sandia Natl Labs, Combust Res Facil, Livermore, CA 94551 USA
[2] Tech Univ Denmark, Dept Chem Engn, DK-2800 Lyngby, Denmark
关键词
D O I
10.1002/(SICI)1097-4601(1999)31:11<757::AID-JCK1>3.0.CO;2-V
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
We have extended our previous kinetic model for the Thermal De-NOx Process to include recent information about the branching fraction alpha(1)(T) of the NH2 + NO reaction, (R1a) NH2 + NO <-> N-2 + H2O (R1b) NH2 + NO <-> NNH + OH where alpha(1)(T) = k(1b)/(k(1a) + k(1b)). The values of the rate coefficients k(1a)(T) and k(1b)(T) used in the model are k(1a) = 2.77 x 10(20) T-2.65 exp(-1258/RT) cm(3)/mole-sec. and k(1b) = 2.29 x 10(10) T-0.425 exp(814/RT) cm(3)/mole-sec. These two rate coefficients combine to give values of the total rate coefficient and branching fraction that are in excellent agreement with experiments over a wide range of temperatures, 300 K < T < 1400 K for k(1) = k(1a) + k(1a) and 300 K < T < 2000 K for alpha(1)(T). The smaller values of alpha(1)(T) in the Thermal De-NOx temperature window, 1100 K < T < 1400 K, used in the model allow us to reduce the value of the NNH lifetime to 1.5 x 10(-8) sec, which is consistent both with the upper limit set by experiment and with the best theoretical predictions. We compare the model predictions with the experiments of Kasuya et al. and discuss the results in some detail. (C) 1999 John Wiley & Sons, Inc.
引用
收藏
页码:757 / 765
页数:9
相关论文
共 50 条
  • [1] Pressure effects on the thermal de-NOx process
    Kjærgaard, K
    Glarborg, P
    Dam-Johansen, K
    Miller, JA
    [J]. TWENTY-SIXTH SYMPOSIUM (INTERNATIONAL) ON COMBUSTION, VOLS 1 AND 2, 1996, : 2067 - 2074
  • [2] Modeling kinetics and mechanisms of important elementary reactions in the thermal De-NOx process.
    Truong, TN
    [J]. ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 1999, 218 : U391 - U391
  • [3] A solution to the problem of large energy consumption of the de-NOX process by non-thermal plasma
    Yoshioka, Y
    Tezuka, T
    [J]. JOURNAL OF ADVANCED OXIDATION TECHNOLOGIES, 2005, 8 (02) : 234 - 240
  • [4] Flow reactor study of the effect of pressure on the thermal De-NOx process
    Schmidt, CC
    Bowman, CT
    [J]. COMBUSTION AND FLAME, 2001, 127 (1-2) : 1958 - 1970
  • [5] Software NOx predictor for control of de-NOx process in power plants
    Fujii, S
    Kang, ZB
    Matsumura, S
    [J]. PROCEEDINGS OF THE 5TH ASIA-PACIFIC CONFERENCE ON CONTROL & MEASUREMENT, 2002, : 68 - 73
  • [6] Study of thermal deactivation of a de-NOx commercial catalyst
    Nova, I
    Acqua, LD
    Lietti, L
    Giamello, E
    Forzatti, P
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 2001, 35 (01) : 31 - 42
  • [7] ON-SITE AMMONIA SYNTHESIS IN De-NOx PROCESS
    Aika, Ken-Ichi
    Kakegawa, Toshiaki
    [J]. CATALYSIS TODAY, 1991, 10 (01) : 73 - 80
  • [8] Non-thermal-plasma-activated de-NOx catalysis
    Gholami, Rahman
    Stere, Cristina E.
    Goguet, Alexandre
    Hardacre, Christopher
    [J]. PHILOSOPHICAL TRANSACTIONS OF THE ROYAL SOCIETY A-MATHEMATICAL PHYSICAL AND ENGINEERING SCIENCES, 2018, 376 (2110):
  • [9] Mechanism study into the combined de-SO2 and de-NOx process in the aqueous solution of heteropoly compound
    Wang, Rui
    Enqiu, Hong
    [J]. ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2006, 231
  • [10] FABRICATION OF A DE-NOX PLANT
    BLANDFORD, KR
    [J]. METAL CONSTRUCTION, 1980, 12 (06): : 274 - 275