That is quite easy once you know condensate mass flow rate. Check the specific volume of steam at the operating temperature from steam tables. For example, at 1210C the specific volume of steam is 0.841 M3/Kg (at a pressure of 2.11 bar a). If your condensate flow rate is, say, 30Kg/Hr then you are evacuating the chamber at a rate of 30 x 0.841 = 25.23 M3/Hr. So that should be the compensation for reduced volume.
If you provide atleast half the flow rate, your chamber will be at atmospheric pressure. (the 25.23M3/Hr flow rate will maintain the chamber at sterilization pressure)
Regards,
Believe it or not : Though human body is made up of intricate and subtle mechanism, it is very poor in energy conversion. The maximum efficiency is 20% during cycling. During under water swimming it is just 4%.