Technical University of Hamburg-Harburg, Fluid Mechanics Department, D-21071, Hamburg, Germany
Abstract:
Pressure relief of a hydrogen peroxide decomposition in a top-vented vessel is simulated numerically using six phase separation models. The results lead to the conclusion that generally a parameter study will be required for relief design by simulation when a gas-generating reaction is considered. None of the phase separation models can be expected to be always conservative in contrast to the case of tempered systems.