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Vapor Pressure of Dichlorosilane, Trichlorosilane, and Tetrachlorosilane from 300 K to 420 K
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    Vapor Pressure of Dichlorosilane, Trichlorosilane, and Tetrachlorosilane from 300 K to 420 K
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    #Centre for Energy and Fluid Science & Resources Division, School of Mechanical & Chemical Engineering, University of Western Australia, Crawley, Western Australia, Australia 6009
    5216 Sun Meadow Drive, Flower Mound, Texas 75022, United States
    § Office of President, Georgia Institute of Technology, Atlanta, Georgia 30332, United States
    LINN Energy Llc, 600 Travis Street, Suite 5100, Houston, Texas 77002, United States
    Chemical Engineering Department, Texas A&M University, College Station, Texas 77843, United States
    Department of Chemical and Process Engineering, University of Canterbury, Christchurch, New Zealand
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    Journal of Chemical & Engineering Data

    Cite this: J. Chem. Eng. Data 2016, 61, 8, 2799–2804
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    https://doi.org/10.1021/acs.jced.6b00142
    Published June 9, 2016
    Copyright © 2016 American Chemical Society

    Abstract

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    The method for the preparation of elemental silicon of sufficient purity for the fabrication of electronic devices is by first converting silicon oxide to silicon–hydrogen-chloride compounds, purifying the material as a fluid mixture, and then converting the product to solid silicon. During the purification process a mixture of dichlorosilane (SiH2Cl2), trichlorosilane (SiHCl3), and tetrachlorosilane or silicon tetrachloride (SiCl4) are formed with each of the components in significant quantities. Models that describe the vapor–liquid equilibrium behavior for the mixtures are required to design appropriate separation and purification processes. Pure fluid properties form the starting point for most mixture models, hence the importance of vapor pressures for the pure materials. In this work we report measurements of the vapor pressures for three of the most important fluids in the silicon production process, dichlorosilane, trichlorosilane, and tetrachlorosilane. Our results are compared with measurements reported previously. The instability of chlorosilanes complicates the experimental procedures because of the corrosive nature of the products formed, and in particular the potential for self-ignition upon exposure to moist air. The experimental procedures used to minimize the hazards and to avoid contamination of the fluids are described.

    Copyright © 2016 American Chemical Society

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    Supporting Information

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    . The Supporting Information is available free of charge on the ACS Publications website at DOI: 10.1021/acs.jced.6b00142.

    • Log p vs 1/T plot showing calculation of extrapolated critical pressure for dichlorosilane, table of estimated critical pressures, and temperatures of dichlorosilane; tables of literature references to vapor pressure data for dichlorosilane, trichlorosilane, and tetrachlorosilane, and tables of literature vapor pressure data including estimated uncertainties (PDF)

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    Cited By

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    This article is cited by 3 publications.

    1. Arman Siahvashi, Saif Z. S. Al-Ghafri, Jordan H. Oakley, Thomas J. Hughes, Brendan F. Graham, and Eric F. May . Visual Measurements of Solid–Liquid Equilibria and Induction Times for Cyclohexane + Octadecane Mixtures at Pressures to 5 MPa. Journal of Chemical & Engineering Data 2017, 62 (9) , 2896-2910. https://doi.org/10.1021/acs.jced.7b00171
    2. Ralf Dohrn, Stephanie Peper, Catinca Secuianu, José M.S. Fonseca. High-pressure fluid-phase equilibria: Experimental methods, developments and systems investigated (2013–2016). Fluid Phase Equilibria 2024, 579 , 113978. https://doi.org/10.1016/j.fluid.2023.113978
    3. Shuzo Ohe. A prediction method of vapor pressures by using boiling point data. Fluid Phase Equilibria 2019, 501 , 112078. https://doi.org/10.1016/j.fluid.2019.01.018

    Journal of Chemical & Engineering Data

    Cite this: J. Chem. Eng. Data 2016, 61, 8, 2799–2804
    Click to copy citationCitation copied!
    https://doi.org/10.1021/acs.jced.6b00142
    Published June 9, 2016
    Copyright © 2016 American Chemical Society

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