rose55
Chemical
- Apr 11, 2010
- 2
Consider a tank rated at 50 psig MAWP and containing a hydrocarbon at 50% level and heated externally such that the vapor pressure in the tank is about 10 psig. Not exactly a flash tank, but similar. The supply source (60 psig from pump) delivers hydrocarbon to the tank at elevated temperature, with some flashing of liquid into the tank. Heat is applied to generate more vaporization.
Question: If the vapor valve to the column is accidentally closed and tank pressure is 10 psig, one PSV scenario is obviously continued heat input into the tank causing pressure to exceed PSV set pressure. Ignoring the external heat input into the tank for the moment, is there a second case associated with hydraulics from the supply source being 60 psig, or will liquid flow stop when the vapor valve is closed? Is it possible to get any additional liquid into the tank due to the supply pressure being 60 psig, thereby compressing the vapor space until reaching the supply pressure?
Rose55
Question: If the vapor valve to the column is accidentally closed and tank pressure is 10 psig, one PSV scenario is obviously continued heat input into the tank causing pressure to exceed PSV set pressure. Ignoring the external heat input into the tank for the moment, is there a second case associated with hydraulics from the supply source being 60 psig, or will liquid flow stop when the vapor valve is closed? Is it possible to get any additional liquid into the tank due to the supply pressure being 60 psig, thereby compressing the vapor space until reaching the supply pressure?
Rose55