Ludwig's Applied Process Design for Chemical and Petrochemical Plants, Volume 1, Fourth Edition

Figure 9-14a, Operational Check Sheet [33], lists 16 possible causes of overpressure in a process system and Figure 9-14b shows a typical relief valve process data sheet. There are many others, and each system should be reviewed for its peculiarities. System evaluation is the heart of a realistic, safe, and yet economical overpressure protection installation on any single equipment or any group of equipment. Solving formulas with the wrong basis and/or data can be disastrous. The following should be reviewed:
the sources of possible overpressure
maximum overpressure possible from all sources
maximum rate of volume increase at the burst pressure, and temperature at this condition
length of duration of overpressure.