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    Absorption kinetics of mercury (II) chloride into water and aqueous sodium chloride solution

    Access Status
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    Authors
    Kho, F.
    Pham, Gia
    Date
    2018
    Type
    Journal Article
    
    Metadata
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    Citation
    Kho, F. and Pham, G. 2018. Absorption kinetics of mercury (II) chloride into water and aqueous sodium chloride solution. Fuel Processing Technology. 174: pp. 78-87.
    Source Title
    Fuel Processing Technology
    DOI
    10.1016/j.fuproc.2018.02.017
    ISSN
    0378-3820
    School
    WASM: Minerals, Energy and Chemical Engineering (WASM-MECE)
    URI
    http://hdl.handle.net/20.500.11937/67230
    Collection
    • Curtin Research Publications
    Abstract

    Mercury has been reported to be naturally occurring trace contaminant in the oil and gas reservoirs. In this study, the absorption characteristic of mercury (II) chloride (HgCl 2 ) in water and aqueous sodium chloride (NaCl) solution was investigated. The kinetic parameters of the reaction between HgCl 2 and NaCl is reported for the first time. A semi-batch reactor is used in this work to investigate the absorption process. The solid vaporization method is applied to generate HgCl 2 gas at different concentrations for this study. At the same hydrodynamic condition, the absorption flux of HgCl 2 into water increases from 6.02 × 10 -6 to 10.26 × 10 -6 mol/m 2 .h when absorption temperature is increased from 298 to 333 K. Applying the two-film theory, the absorption of HgCl 2 into water is controlled by the gas phase resistance. The mass transfer coefficient k G does not change with the HgCl 2 concentration in the gas phase significantly, but is affected by the absorption temperature. For the case of absorption of HgCl 2 into aqueous NaCl solution, the absorption flux increases with increasing NaCl concentration and absorption temperature. The mechanism of reaction between HgCl 2 and NaCl is proposed and the reaction rate law follows second order; first order with respect to HgCl 2 and Cl - with the reaction rate constant k 2 =1.09×10 9 exp[Formula presented] m 3 /mol·s.

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