We consider horizontal static liquid layers on planar solid boundaries and analyse their instabilities. The layers are either evaporating, when the plates are heated, or condensing, when the plates are cooled. Vapour recoil, thermocapillary, and rupture instabilities are discussed, along with the effects of mass loss (or gain) and non-equilibrium thermodynamic effects. Particular attention is paid to the development of dryout. We derive long-wave evolution equations for the interface shapes that govern the two-dimensional nonlinear stability of the layers subject to the above coupled mechanisms. These equations are analysed and their predictions discussed. Previous theoretical and experimental results are reviewed and compared with the present results. Finally, we discuss limitations of the modelling and extend our derivation to the case of three-dimensional disturbances.

To honor the memory of our friend and colleague Mikhail Ivanov a review of his great contributions to the understanding of the various phenomena associated with steady-flow shock wave reflection is presented. Of course, he has contributed much more widely than that, but I will restrict myself to this part of his work, because it is what I understand best. In particular, his computational and experimental demonstration of hysteresis in the transition between regular and Mach reflection, and his resolution of the difficulties associated with the triple point in weak Mach reflection in terms of the effects of viscosity and heat conduction are reviewed. Finally, some experimental results are presented that demonstrate that, in the dual-solution domain, Mach reflection is more stable than regular reflection.

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Thermal hazards screening can be quickly and cost‐effectively performed to obtain the required data for the safe scale‐up of chemical processes and to accommodate changes to process recipes. Before scale‐up, it is vital to identify safe temperature and pressure operating ranges, quantify the heat generated from a reaction, and the number of moles of gas generated. It is also prudent to determine the heat and gas generation rates to safely accommodate the reaction in the given process equipment. These rate data can also be used to verify the adequacy of the existing pressure relief system design. Process Hazard Analysis (PHA) and Hazard and Operability (HAZOP) reviews identify credible upset scenarios, and data are required to address these issues. When a process recipe or batch size is changed, data are necessary to quantify the effect of the change on the above parameters. For modifications to existing processes, a management of change review should occur. Data addressing issues resulting from these reviews are readily available by performing calorimetry experiments with the Advanced Reactive System Screening Tool and similar calorimeters. Examples of these applications are included in this article. © 2008 American Institute of Chemical Engineers Process Saf Prog, 2009