Mak,
I tend to disagree with the above advice, as the steam out condition is not necessarily a design condition, but a design verification condition. In no case, the steam out condition would refer to external pressure, unless the Client specification clearly mentioned the partial or full vacuum condition as a consequence of steam out process (in case of blocked vents, the condensing steam may generate a vacuum in the vessel). In your case the the external pressure has been nominated FV, but the internal pressure of 0.5 kgf/cm2 (please note that the steam is applied inside the vessels for clean-out purposes) is less than the design pressure, hence no effect on the vessel components. However the steam out temperature may affect other components, say during an earthquake the excess temperature could affect adversely the support design...So in the loading conditions, you may include the 230 deg C for the supports check, with 0.5 barg internal pressure, instead of the design or operating pressure.
cheers,
gr2vessels