Continuous degradation of 1,4-dioxane by the combination of a stripping column and photo-Fenton reaction in a continuous stirred tank reactor

被引:1
|
作者
Ito, Kohei [1 ]
Matsuoka, Taiki [1 ]
Morisada, Shintaro [1 ]
Ohto, Keisuke [1 ]
Kawakita, Hidetaka [1 ]
Watabe, Yoshihide [2 ]
Higashi, Kotaro [3 ]
Nagamatsu, Shigeki [3 ]
机构
[1] Saga Univ, Fac Sci & Engn, Dept Appl Chem, Saga 8408502, Japan
[2] AGI Glassplant Inc, 1978 Takahama, Arao 8640025, Japan
[3] JEPLAN Inc, 12-2 Ogimachi,Kawasaki Ku, Kawasaki, Kanagawa 2100867, Japan
来源
关键词
4-Dioxane; Degradation; Stripping column; Photo -Fenton reaction; Combined process; 1; DECOMPOSITION; UV;
D O I
10.1016/j.cherd.2023.07.017
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
1,4-Dioxane is a toxic chemical that is used in the chemical industry. The limit concentration of 1,4-dioxane in environment was set at 0.3 mg/kg. Here, for efficient degradation of 1,4-dioxane, combined use of a stripping column and a continuous stirred tank reactor (CSTR) is proposed. The stripping column concentrates 1,4-dioxane, and photo-Fenton reaction in the CSTR decomposes 1,4-dioxane by OH radicals generated by an ultraviolet lamp. In the photo-Fenton reaction, the pseudo-first-order reaction constant was determined to be 1.88 x 10-4 1/s at 318 K. The separation coefficient of 1,4dioxane, the ratio of the concentrations at the top and bottom of the stripping column, was approximately 500-2700 depending on the heat supplied to the column. The optimum combination of the stripping column and CSTR was investigated on the basis of three proposed models. The order of degradation in the CSTR followed by concentration in the stripping column, along with circulation from the top of the column to the CSTR, gave an overall reaction percentage of 99.9%. From energy calculation, a higher separation coefficient (alpha) decreased the total heat duty from 4.5 x 104 J/min at alpha = 640-1.2 x 104 J/min at alpha = 2400. A stripping column for concentration of 1,4-dioxane combined with a CSTR for photo-Fenton reaction shows potential for efficient degradation of 1,4-dioxane. (c) 2023 Institution of Chemical Engineers. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:65 / 73
页数:9
相关论文
共 50 条
  • [41] Fenton's oxidation using iron-containing activated carbon as catalyst for degradation of p-nitrophenol in a continuous stirred tank reactor
    Rodrigues, Carmen S. D.
    Soares, O. S. G. P.
    Pereira, M. Fernando R.
    Madeira, Luis M.
    JOURNAL OF WATER PROCESS ENGINEERING, 2021, 44
  • [42] A CONTINUOUS STIRRED TANK REACTOR INVESTIGATION OF THE GAS-PHASE REACTION OF HYDROXYL RADICALS AND TOLUENE
    GERY, MW
    FOX, DL
    JEFFRIES, HE
    STOCKBURGER, L
    WEATHERS, WS
    INTERNATIONAL JOURNAL OF CHEMICAL KINETICS, 1985, 17 (09) : 931 - 955
  • [43] THE EFFECT OF MICROMIXING ON THE CONVERSION OF THE AUTOCATALYTIC REACTION IN A CONTINUOUS STIRRED-TANK REACTOR WITH PREMIXED FEEDSTREAM
    SAWINSKY, J
    BALINT, A
    BENDE, S
    CHEMICAL ENGINEERING SCIENCE, 1983, 38 (08) : 1355 - 1356
  • [44] REACTION INVARIANTS AND THEIR IMPORTANCE IN ANALYSIS OF EIGENVECTORS, STATE OBSERVABILITY AND CONTROLLABILITY OF CONTINUOUS STIRRED TANK REACTOR
    FJELD, M
    ASBJORNS.OA
    ASTROM, KJ
    CHEMICAL ENGINEERING SCIENCE, 1974, 29 (09) : 1917 - 1926
  • [46] Three limit cycles for a first‐order exothermic chemical reaction in a continuous stirred‐tank reactor
    E. Sáez
    I. Szántó
    A. Monsalve
    Journal of Mathematical Chemistry, 2000, 27 : 171 - 182
  • [47] SUSTAINED AND DAMPED OSCILLATIONS IN THE PERMANGANATE HYDROXYLAMINE REACTION IN A CONTINUOUS-FLOW STIRRED TANK REACTOR
    NAGY, A
    OLEXOVA, A
    TREINDL, L
    JOURNAL OF PHYSICAL CHEMISTRY, 1991, 95 (15): : 5809 - 5810
  • [48] Polymerization of acrylonitrile in the Belousov-Zhabotinsky reaction in a continuous-flow stirred tank reactor
    Washington, R
    Pojman, J
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 1996, 212 : 84 - PHYS
  • [49] Heterogeneous Fenton's oxidation using Fe/ZSM-5 as catalyst in a continuous stirred tank reactor
    Queiros, Samuel
    Morais, V.
    Rodrigues, Carmen S. D.
    Maldonado-Hodar, F. J.
    Madeira, Luis M.
    SEPARATION AND PURIFICATION TECHNOLOGY, 2015, 141 : 235 - 245
  • [50] Kinetic model of photo-Fenton degradation of paracetamol in an annular reactor: main reaction intermediates and cytotoxicity studies
    Gimenez, Barbara N.
    Conte, Leandro O.
    Audino, Francesca
    V. Schenone, Agustina
    Graells, Moises
    Alfano, Orlando M.
    Perez-Moya, Montserrat
    CATALYSIS TODAY, 2023, 413