Ric
Well-Known Member
As any fule no, flooding is proportional to the square of the diameter of the hole and the square root of its depth. Unfortunately most of the calculators found on the net use consistent units (either SI system or Imperial) which makes it difficult to work out whether your bilge pumps can cope with a through hull failure. Most bilge pumps are rated in USG/Hour, we still use inches for through hull diameters, but I at least am metric for depths. So boiling it all down I calculated that flooding (measured in USG/Hour) is equal to 2128 x root of through hull depth (m) x square of through hull diameter (inches).
With that formula you can work out whether your bilge pumps can cope with a through hull failure. Obviously the bilge pump probably won't pump at its rated value due to head, voltage drop, pipe skin friction, check valves etc, but it should give you something to work with.
As an example, my worst case through hull failure would be my sink outlet (1" through hull with outlet 0.15m below waterline, giving a flood rate of 824USG/hour. I have two bilge pumps, one nominally rated at 500USG/Hour, the other at 1100USG/hour. I am thus reasonably confident that my pumps can cope with the worst case failure.
Hope it helps!
With that formula you can work out whether your bilge pumps can cope with a through hull failure. Obviously the bilge pump probably won't pump at its rated value due to head, voltage drop, pipe skin friction, check valves etc, but it should give you something to work with.
As an example, my worst case through hull failure would be my sink outlet (1" through hull with outlet 0.15m below waterline, giving a flood rate of 824USG/hour. I have two bilge pumps, one nominally rated at 500USG/Hour, the other at 1100USG/hour. I am thus reasonably confident that my pumps can cope with the worst case failure.
Hope it helps!