continue to increase.) Static head is found
simply by measuring the appropriate vertical
distances in feet or meters.
In a system that circulates water, like a
closed cooling system, there is no static head.
The water begins and ends its travel at the
same level—at the pump.
Velocity Head
Velocity head is the head that results from the
kinetic energy in the water flow. It is the head
(height) the water would have to fall from to
reach the velocity it’s moving at in the sys-
tem. Velocity head is important for high-
volume systems, but at under 200 gpm or
12,000 gph (760 lpm or 45,600 lph), velocity
head is small, usually under 0.4 foot (0.12 m).
For our purposes here, we can ignore it.
Pressure Head
In Figures 19-6 and 19-7, we are pumping to
and from open containers. The height of the
water in the container we’re pumping into
(above the pipe’s inlet) is the pressure head,
but it is already taken into account in the
height of the discharge head. If you want a
given pressure at a nozzle outlet for, say, a
fire hose or a deck washdown, you can con-
vert the required pressure in psi or kPa to
head in feet or meters and add it to the total
required head.
head (fresh water), ft. ÷ 2. 31 =psi
psi × 2. 31 =head (fresh water), ft.
or
head (fresh water), m × 9. 8 =kPa
kPa ÷ 9. 8 =head (fresh water), m
Seawater is 1.028 times denser, but for most
ordinary pump calculations this can be neg-
lected for static head and pressure head.
A bilge pump simply pumps into the at-
mosphere. You don’t care about the exit pres-
sure, only the flow rate, so the pressure head
is zero. However, if you are selecting a pump
to fill a tank and the pipe inlet is near the bot-
tom of the tank, you will have to add the pres-
sure head, either by accounting for the total
height of water in the tank as static head or
by adding it separately as pressure head.
(Note that such a pipe to the bottom of a tank
would require a check valve.)
Friction Head
As water flows through pipes and fittings, it
loses energy due to the friction of rubbing
against the pipe walls. All pumps must over-
come this significant component of the
head. It has to be taken into account in any
piping system. The longer the pipe run and
the more fittings or bends, the greater the
friction head. Similarly, for a given flow of
water, the larger the pipe diameter and the
fewer the fittings or bends, the less the fric-
tion head.
Calculating Friction Head
Friction head can be calculated as follows.
Formula 19-1. Friction Head
or
Where
hf =friction head, ft. or m
L =total length of pipe, ft. or m
gpm =flow, gallons per minute
lpm =flow, liters per minute
ID =inside diameter of pipe, in. or cm
(NOTE: ID in cm, notmm, in this
formula)
C =coefficient of roughness for the type
of pipe:
Iron and Steel Pipe = 100
Plastic, Lead, Copper, and Brass Pipe =
130
Smooth Hose = 140
Corrugated Hose = 150
Friction head from fittings can be deter-
mined from Table 19-2.
To determine the total friction head in the
system, you list all the fittings and then multiply
them by their equivalent lengths. For instance, a
90-degree elbow is 30 D; for a 1^1 / 4 - inch pipe, its
equivalent length is 37. 5 inches or 3.125 feet; for
hf, m
82 .54 L, m lpm
C (ID, c m)
1. 85
= 1. 85 4. 86
××
×
hf, ft.
10 .44 L, ft. gpm
C(ID,in.)
1. 85
= 1. 85
××
×^44.^86
PART SIX:PLUMBING SYSTEMS WITH NOTES ON FIRE SUPPRESSION
Formula 19-1.