Q2. As a part of an Oil Company's Process Safety plan, crude oil tank fire scenario can be mitigated by pumping the tank empty in 1 hour. The crude oil is at a 9m level, with the tank diameter being 30m. It is planned pump the oil through a 200mm ID new commercial steel pipe (ε = 0.046mm) to another tank 40m in diameter and 10m high. The pipeline runs to an equivalent length of 50m. a. In the time mentioned above, what minimum pump size (in HP) would be required to pump the tank empty. Assume pump efficiency of 80%. b. If a 100 HP (80% efficient) pump is available, how long will it take to empty the tank? c. What conclusions can be drawn about the viability of this approach? What kind of hazards can be foreseen in this operation from a process safety perspective? What can be a probable initiating cause of an accident? What can be a suggestion to mitigate the risks? Density: 928 kg/m³, Viscosity: 0.004 kg/m-s

Elements Of Electromagnetics
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Author:Sadiku, Matthew N. O.
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Q2. As a part of an Oil Company's Process Safety plan, crude oil tank fire scenario can be mitigated by pumping
the tank empty in 1 hour. The crude oil is at a 9m level, with the tank diameter being 30m. It is planned pump
the oil through a 200mm ID new commercial steel pipe (e = 0.046mm) to another tank 40m in diameter and 10m
high. The pipeline runs to an equivalent length of 50m.
a. In the time mentioned above, what minimum pump size (in HP) would be required to pump the tank
empty. Assume pump efficiency of 80%.
b. If a 100 HP (80% efficient) pump is available, how long will it take to empty the tank?
c. What conclusions can be drawn about the viability of this approach? What kind of hazards can be
foreseen in this operation from a process safety perspective? What can be a probable initiating cause of
an accident? What can be a suggestion to mitigate the risks?
Density: 928 kg/m', Viscosity: 0.004 kg/m-s
Transcribed Image Text:Q2. As a part of an Oil Company's Process Safety plan, crude oil tank fire scenario can be mitigated by pumping the tank empty in 1 hour. The crude oil is at a 9m level, with the tank diameter being 30m. It is planned pump the oil through a 200mm ID new commercial steel pipe (e = 0.046mm) to another tank 40m in diameter and 10m high. The pipeline runs to an equivalent length of 50m. a. In the time mentioned above, what minimum pump size (in HP) would be required to pump the tank empty. Assume pump efficiency of 80%. b. If a 100 HP (80% efficient) pump is available, how long will it take to empty the tank? c. What conclusions can be drawn about the viability of this approach? What kind of hazards can be foreseen in this operation from a process safety perspective? What can be a probable initiating cause of an accident? What can be a suggestion to mitigate the risks? Density: 928 kg/m', Viscosity: 0.004 kg/m-s
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