Adsorption of elemental mercury vapor by impregnated activated carbon from a commercial respirator cartridge

被引:18
作者
Chung, Sang Tae [1 ]
Kim, Kwang Il [1 ]
Yun, Yu Ran
机构
[1] Inje Univ, Dept Occupat Hlth & Safety Engn, Gimhae, South Korea
关键词
Impregnated activated carbon; Mercury adsorption; Adsorption model; Mercury breakthrough; Respirator cartridge; PARTICLES; BEDS; HEAT;
D O I
10.1016/j.powtec.2008.11.012
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In order to protect workers from the harmful effects of mercury vapor, adsorption technology using impregnated activated carbon is currently in use in respirator cartridges to capture mercury vapor in breathing air. Adsorption onto the activated carbon can be improved through the modification of the carbon surface by impregnation with certain reagents that enhance the bonding of mercury either physically or chemically. The first objective of this study was to characterize the chemisorption behavior of a commercial adsorbent (3M-6009) by measuring the mercury breakthrough using a bench-top apparatus. The second objective was to develop a kinetic model describing the breakthrough behavior. Dynamic breakthrough concentrations were measured using a fixed bed to study the effects of the following adsorption parameters at room temperature: air flow-rate, adsorbent amount, inlet mercury concentration, and bed diameter. A model was developed in which, the rate of irreversible chemisorption was proportional to the concentration of mercury in the airflow, and the concentration of active sites of the surface of the carbon. A model incorporating two different types of the active sites was applied in an effort to differentiate the high initial adsorption rate mediated by readily accessible open sites from the lower adsorption rate mediated by the availability of hindered sites within micro-pores. The model developed herein was superior to a traditional isotherm model for describing the chemisorption behavior of impregnated activated carbon. (c) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:47 / 53
页数:7
相关论文
共 18 条
  • [1] HEAT AND MASS TRANSFER IN FIXED AND FLUIDIZED BEDS OF LARGE PARTICLES
    BRADSHAW, RD
    MYERS, JE
    [J]. AICHE JOURNAL, 1963, 9 (05) : 590 - 595
  • [2] GEANKOPLIS CJ, 1993, TRANSPORT PROCESSES, P447
  • [3] Gupta A. S., 1962, AICHE J, V8, P608, DOI DOI 10.1002/AIC.690080509
  • [4] TRANSITIONAL BEHAVIOR FOR SIMULTANEOUS MASS + HEAT TRANSFER OF GASES FLOWING THROUGH PACKED + DISTENDED BEDS OF SPHERES
    GUPTA, AS
    THODOS, G
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1964, 3 (03): : 218 - &
  • [5] Simulation of mercury emission control by activated carbon under confined-bed operations
    Ho, T. C.
    Shetty, S.
    Chu, H. W.
    Lin, C. J.
    Hopper, J. R.
    [J]. POWDER TECHNOLOGY, 2008, 180 (03) : 332 - 338
  • [6] Karatza D, 1996, TWENTY-SIXTH SYMPOSIUM (INTERNATIONAL) ON COMBUSTION, VOLS 1 AND 2, P2439
  • [7] Study of mercury absorption and desorption on sulfur impregnated carbon
    Karatza, D
    Lancia, A
    Musmarra, D
    Zucchini, C
    [J]. EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2000, 21 (1-3) : 150 - 155
  • [8] SORPTION OF ELEMENTAL MERCURY BY ACTIVATED CARBONS
    KRISHNAN, SV
    GULLETT, BK
    JOZEWICZ, W
    [J]. ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1994, 28 (08) : 1506 - 1512
  • [9] MCCABE WL, 1993, UNIT OPERATIONS CHEM, P666
  • [10] MCCABE WL, 1993, UNIT OPERATIONS CHEM, P671