Supercritical water oxidation of feeds with high ammonia concentrations Pilot plant experimental results and modeling

被引:63
作者
Bermejo, M. D. [1 ]
Cantero, F. [1 ]
Cocero, M. J. [1 ]
机构
[1] Univ Valladolid, High Pressure Proc Grp, Dept Chem Engn & Environm Technol, E-47011 Valladolid, Spain
关键词
supercritical water oxidation; ammonia; isopropyl alcohol; cooling wall reactor; pilot plant; reactor modeling;
D O I
10.1016/j.cej.2007.05.010
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Supercritical water oxidation (SCWO) is an effective method for the treatment of industrial wastes. SCWO of organic compounds containing nitrogen, found frequently in industrial wastes, results in the rapid conversion into molecular nitrogen without generation of NO.. The stable intermediate in the SCWO of nitrogenous compounds is ammonia. Thus, SCWO of feeds with high ammonia concentrations is studied, in order to make the process more efficient and energetically profitable. All the experiments presented have been performed using the cooling wall reactor at pilot plant scale. Several feeds with concentrations of ammonia up to 7 wt.% have been oxidized using isopropyl alcohol (IPA) as a fuel. Results show that total ammonia removal is possible, even at high concentrations, with stoichiometric air quantity and residence times of 40 s. In our reactor, keeping the feed flow constant, that is keeping the residence time approximately constant between 35 and 45 s, the reaction temperature necessary for reaching the complete TOC and NH3 removal is higher when the ammonia concentration is increased: 710 degrees C for I wt.% of NH3, and 780 degrees C for 7 wt.% of NH3. A theoretical study of the experimental results has been performed using a simple flow patterns model specifically developed for this reactor, based on an extensive literature search of ammonia destruction kinetics. (C) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:542 / 549
页数:8
相关论文
共 25 条
  • [1] EQUATION-OF-STATE REPRESENTATION OF PHASE-EQUILIBRIA AND VOLUMETRIC PROPERTIES OF THE SYSTEM NACL-H2O ABOVE 573-K
    ANDERKO, A
    PITZER, KS
    [J]. GEOCHIMICA ET COSMOCHIMICA ACTA, 1993, 57 (08) : 1657 - 1680
  • [2] Detailed chemical kinetic modeling of methylamine in supercritical water
    Benjamin, KM
    Savage, PE
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (26) : 9785 - 9793
  • [3] Supercritical water oxidation of methylamine
    Benjamin, KM
    Savage, PE
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (14) : 5318 - 5324
  • [4] Modeling of a transpiring wall reactor for the supercritical water oxidation using simple flow patterns:: Comparison to experimental results
    Bermejo, MD
    Fernández-Polanco, F
    Cocero, MJ
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (11) : 3835 - 3845
  • [5] Optimisation of the operation variables of a supercritical water oxidation process
    Cocero, MJ
    Vallelado, D
    Torío, R
    Alonso, E
    Fdez-Polanco, F
    [J]. WATER SCIENCE AND TECHNOLOGY, 2000, 42 (5-6) : 107 - 113
  • [6] Supercritical water oxidation in a pilot plant of nitrogenous compounds:: 2-propanol mixtures in the temperature range 500-750 °C
    Cocero, MJ
    Alonso, E
    Torío, R
    Vallelado, D
    Fdz-Polanco, F
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (10) : 3707 - 3716
  • [7] Reactions nitrate salts with ammonia in supercritical water
    DellOrco, PC
    Gloyna, EF
    Buelow, SJ
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (07) : 2547 - 2557
  • [8] Supercritical water oxidation of NH3 over a MnO2/CeO2 catalyst
    Ding, ZY
    Li, LX
    Wade, D
    Gloyna, EF
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (05) : 1707 - 1716
  • [9] GIDNER A, 1999, P 6 M SUP FLUIDS CHE
  • [10] Goto R, 1999, IND ENG CHEM RES, V38, P4500