Hi Jasper,
I have a quick question (I hope). I'd like to run a parametric study in which I vary the operating pressure of the NH3 synthesis loop. However, the loop contains both a feed compressor, and a recycle compressor. Thus, if I vary only the recycle, then it's not representative of a real plant. Is it possible to link the two compressors with a controller? For example, if the feed is at 180bar, then the recycle knows to be at 180 bar as well. I'd like to do this to see how the compressor power requirements (i.e. cost) change with pressure. It also gives a cost for the net energy if some $/kWh is assumed.
Thanks,
Eric