Calculation of the Claus reaction involving aminoacidic gases
Thread Content
In the hydrogen sulfide-containing acidic gas treated by the Claus process, the H2S content is 15% and the NH3 content is 30%. There is an ammonia decomposition catalyst in the reactor; under such conditions, how can Aspen or VMG be used to simulate the reaction conditions in the reactor and calculate the material balance there?
Aspen cannot be used for simulation; VMG, on the other hand, has specialized sulfur packages and modules to simulate the reaction conditions in reactors
The models in VMG are unable to handle the reaction of NH3
But the electrolyte model in Aspen isn’t suitable for such high temperatures, right?