Experimental study of the vapour-liquid equilibria of HI-I sub(2-H) sub(2)O ternary mixtures, Part 2: Experimental results at high temperature and pressure

In order to assess the choice of the sulphur-iodine thermochemical cycle for massive hydrogen production, a precise knowledge of the concentrations of the gaseous species (HI, I sub(2, and H) sub(2)O) in thermodynamic equilibrium with the liquid phase of the HI-I sub(2-H) sub(2)O ternary mixture is required, in a wide range of concentrations and for temperatures and pressures up to 300 degree C and 50 bar. In the companion paper (Part 1) the experimental device was described, which enables the measurement of the total pressure and concentrations of the vapour phase (and thus the knowledge of the partial pressures of the different gaseous species) for the HI-I sub(2-H) sub(2)O mixture in the 20-140 degree C range and up to 2 bar. This (Part 2) article describes the experimental device which enables similar measurements but now in the process domain. The results concerning concentrations in the vapour phase for the HI-I sub(2-H) sub(2)O initial mixture (with a global composition) in the 120-270 degree C temperature range and up to 30 bar are presented. As previously, optical online diagnostics are used, based on recordings of infrared transmission spectra for HI and H sub(2O and on UV/visible spectrometry for I) sub(2). The concentrations measured in the vapour phase are the first to describe the vapour composition under thermophysical conditions close to those of the distillation column. The experimental results are compared with a thermodynamic model and will help us to scale up and optimize the reactive distillation column we promote for the HI section of the sulphur-iodine cycle.