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CEA 4001 - Suction conditions

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60
9.6.1 General
Wherever
possible,
horizontal
centrifugal
pumps
should
be
used,
installed
with
a
positive
suction
head.
i.e.
in
accordance
with
the
following:
-
At
least
two
thirds
of
the
effective
capacity
of
the
suction
tank
shall
be
above
the
level
of
the
pump
centre
line;
-
The
pump
centre
line
shall
be
no
more
than
2
m
above
the
low
water
level
of
the
suction
tank
(level
X
in
8.3.5).
NOTE:
If
this
is
not
feasible,
the
pump
may
be
installed
under
suction
lift
conditions
or
vertical
turbine
pumps
may
be
used.
NOTE:
Suction
lift
and
submersible
pump
arrangements
should
be
avoided
and
only
used
when
it
is
not
practicable
to
arrange
positive
suction
head.
It
is
critical
that
suction
lift
arrangements
should
not
vary
from that
stated
in
9.6.2
and
as
shown
in
figures
5
and
6.
9.6.2
Suction
pipe
9.6.2.1
General
The
pump
suction
shall
be
connected
to
a
straight
or
taper
pipe
at
least
two
diameters
long.
The
taper
pipe shall
have
horizontal
topside
and
a
maximum
included
angle
not
exceeding
20ยบ.
Valves
shall
not
be
fitted directly
to
the
pump
inlet.
The
suction
piping,
including
all
valves
and
fittings,
shall
be
designed
in
such
a
way
as
to
ensure
that
the available
NPSH
at
the
pump
inlet
exceeds
the
required
NPSH
by
at
least
1
m
with
the
maximum
demand flow
and
maximum
water
temperature
(see
table
15).
T
Table 15: Pump pressure and flow rating
Pipework
Hazard
Class
Rated
pump
flow
Pump
inlet
condition
Pre-calculated
LH/OH
Maximum
demand
flow
from
table
7
For
tanks,
with
water
supp
ly
at
low
water level
(see
X
in
Figure
4). For
b
ooster
pumps,
with
mi
nimum
town
main
pressure.
HH
1,4
x
Flow
Required
from
table
8
Fully
calculated
All
Maximum
demand
flow
Suction
piping
shall
be
laid
either
horizontal
or
with
a
continuous
slight
rise
towards
the
pump
to
avoid
the possibility
of
air
locks
forming
in
the
pipe.
A
foot
valve
shall
be
fitted
where
the
centre
line
of
the
pump
is
above
the
low
water
level
(see
8.3.5).
9.6.2.2 Positive head
The
diameter
of
the
suction
pipe
shall
be
no
less
than
65
mm.
Furthermore,
the
diameter
shall
be
such
that
a velocity
of
1,8
m/s
is
not
exceeded
when
the
pump
is
operating
at
maximum
demand
flow.
This
velocity may
be
increased
to
2,5m/s,
if
the
pressure
in
the
suction
pipe
is
not
more
than
0,4
bar
below
ambient pressure.

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