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Platinum Metals Rev., 1971, 15, (3), 92

Fugacity of Hydrogen in Gas Mixtures

The Use of Silver-Palladium Membranes

  • By A. B. Ghosal
  • A. E. Klink
  • Columbia University, New York
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A 25 per cent silver-palladium membrane has been successfully used in this laboratory (1, 5, 6) to directly determine the fugacities of hydrogen in hydrogen-containing fluid mixtures. This application depends on the fact that this alloy is permeable only to hydrogen and has been commercially used to prepare ultra-high purity hydrogen. Some information is available on various aspects of the diffusion of hydrogen through silver-palladium alloy membranes. This includes the effects of temperature, pressure (2) and water vapours (7) on the diffusion rate, solubility of hydrogen in palladium alloys (4, 8), maintenance of dimensional stability (3), and fabrication techniques (1).

In the present series of investigations pure hydrogen is maintained on one side of the membrane and on the other side is a mixture containing hydrogen. At equilibrium through equality of chemical potentials, the fugacity of pure hydrogen at the temperature and equilibrium pure hydrogen pressure is equal to the fugacity of hydrogen at the same temperature and equilibrium mixture pressure and composition. The fugacity of the pure hydrogen can be readily and accurately calculated from the P-V-T data on hydrogen. The technique therefore provides a powerful tool to directly determine fugacities of hydrogen as a component in a mixture without having to determine the partial molar volumes (a laborious and tedious way) and also serves as a means of evaluating the various predictive methods such as the equations of state as applied to mixtures.

The equipment consists of the palladium-silver membrane, which is in the form of a coil made of 40 feet of 25 per cent silver-palladium tubing, 0.063 in. o.d. and 0.003 in. wall. This coil is located inside a high pressure vessel which is maintained at constant temperature by an oil bath. The coil is brazed with a short piece of nickel tube ( in. o.d.) at one end and sealed at the other. The nickel tube is connected by a swage-lock fitting to a stainless steel fitting welded to a stainless steel manifold plate. The manifold plate closes the mouth of the pressure vessel which is equipped with a suitable enclosure cap and gaskets to ensure a leak-proof closure. The system has provisions for evacuating, charging gases to either side of the membrane separately and for sampling for analysis. This cell is kept at constant uniform temperature and the pressures on two sides of the membrane are measured separately by a standard dead weight piston gauge assembly provided with diaphragm null pressure indicators.

The studies made so far include determination of fugacities of hydrogen in the hydrogenpropane system (1, 5) up to 138°C and a mixture pressure of 2500 p.s.i.a., the hydrogen-butane system in the single phase (5) and two phase (6) regions and the hydrogenpropane-butane ternary system (5). In the study of the vapour-liquid system it is important to note that at equilibrium the fugacity of pure hydrogen in the tube is equal to the fugacity of the hydrogen in both the liquid and the vapour mixtures.

In conclusion, we evaluate the vapour and the liquid phase thermodynamic properties by directly measuring the fugacity of hydrogen in the hydrogen-hydrocarbon mixtures. We do this by using a silver-palladium membrane permeable only to hydrogen.

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References

  1. 1
    H. W. Cooper, Eng. Sc.D. Thesis, Columbia University Chemical Engineering Department, “The Determination of the Fugacities of Hydrogen in Hydrogen and Propane Mixtures Using a Semipermeable Membrane”, 1967
  2. 2
    P. L. Damour, Ph.D. Thesis, Catholic University of America, “The Effect of Temperature and Pressure on the Maximum Diffusion Rate of Hydrogen through Palladium”, 1962
  3. 3
    A. S. Darling, Johnson Matthey & Co Ltd, British Patent 827,681, “Maintenance of Dimensional Stability in Palladium Diffusion Membranes”
  4. 4
    T. B. Flanagan, J. Phys. Chem., 1963, 67, 203
  5. 5
    A. B. Ghosal, Eng. Sc.D. Thesis, Columbia University Chemical Engineering Department, unpublished
  6. 6
    A. E. Klink, Eng. Sc.D. Thesis, Columbia University Chemical Engineering Department, unpublished
  7. 7
    W. F. Reid, Ph.D. Thesis, Catholic University of America, “Influence of Water on the Rate of Transmission of Hydrogen Through Palladium”, 1962
  8. 8
    P. Mitacek and J. G. Aston, J. Am. Chem. Soc., 1963, 85, 137

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