Page 89 - Plant design and economics for chemical engineers

29. FICA-l fails Deadhead pump Damage to pump None See Event 26.
closing FV-1
30. V-3 open Reagent released FICA-1 Estimate release
quantity.
More 31. FV-1 fails open Upset in reactor Reagent released FICA-1 Possible problem
in reactor.
32. FICA-l fails, Upset in reactor Reagent released None See Event 31.
opening FV-1
Pressure
More 33. V-4 closed Deadhead pump Damage to pump PI-l, See Event 26.
FICA-l
34. FV-1 fails closed Deadhead pump Damage to pump PI-l, See Event 26.
FICA-l
35. FICA-1 fails, Deadhead pump Damage to pump PI-1 See Event 26.
closing FV-1
36. V-2 and Deadhead pump Overpressure in PI-l, Evaluate need for
V-4 closed pump or line FICA-l hydraulic relief.
Less 37. V-2 closed Pump cavitates Damage to pump PI-l, See Event 1.
FICA-1
38. V-3 open Reagent released PI-1 See Event 3.
Temperature
More 39. V-4 closed Deadhead pump Damage to pump None See Event 26.
40. FV-1 fails closed Deadhead pump Damage to pump None See Event 26.
41. FICA-l fails, Deadhead pump Damage to pump None See Event 26.
closing FV-1