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The figure below shows the Ammonia process with vapor-liquid equilibrium and a purge stream. Separator Recycle Purge Mixer Flash Separator Reactor Reacting Inlet Product Calculate all the streams inlet and outlet for the mixer, reactor, flash separator and recycle for all components. Set the conversion per pass in the reactor to 25%. Change the separator so that it is a phase separation. The K-values are Nitrogen Hydrogen Ammonia carbon dioxide 4.8 70 0.051 0.32 The flow rates of nitrogen and hydrogen into the process are one and three moles per time unit, respectively, but there is also 0.01 moles per time unit of carbon dioxide. Because of the carbon dioxide, you will add a purge stream as one per cent of the recycle stream