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Type WEH22
WK 460 110 09.2017
- 29 -
O
O
O
Operati
perati
perati
perating
ng
ng
ng lim
lim
lim
limits
its
its
its
PERFORMANCE CURVES
Fl
Fl
Fl
Flo
o
o
ow res
w res
w res
w resiiiist
st
st
sta
aa
ance c
nce c
nce c
nce cur
ur
ur
urves
ves
ves
ves
1 - spool R
R
R
R
- flow direction
B
B
B
B
→
→
→
→
A
A
A
A
2 - spools: E
EE
E
, R
R
R
R
, W
W
W
W
1 - spool SSSS
2 - spools: FFFF, H
H
H
H
, J
J
J
J
, L
L
L
L
, M
M
M
M
, Q
Q
Q
Q
, U
U
U
U
, V
V
V
V
, W
W
W
W
, C
C
C
C
, D
D
D
D
, K
K
K
K
, Z
ZZ
Z, D1
, D1
, D1
, D1
Performance curves
∆∆∆∆
p
p
p
p
(Q
Q
Q
Q
) for directional valves
type ...4
4
4
4W
W
W
WE
EE
EH
H
H
H2
2
2
22
2
2
2
... with spools: E
EE
E
, R
R
R
R
, W
W
W
W
Performance curves
∆∆∆∆
p
p
p
p
(Q
Q
Q
Q
) for directional valves
type ...4
4
4
4W
W
W
WE
EE
EH
H
H
H2
2
2
22
2
2
2
... with spools: G
G
G
G
, T
TT
T
Performance curves
∆∆∆∆
p
p
p
p
(Q
Q
Q
Q
) for directional valves
type ...4
4
4
4W
W
W
WE
EE
EH
H
H
H2
2
2
22
2
2
2
... with spools:
FFFF
,
H
H
H
H
,
JJJJ
,
LLLL
,
M
M
M
M
,
Q
Q
Q
Q
,
S
SS
S
,
U
U
U
U
,
V
V
V
V
,
W
W
W
W
,
D
D
D
D
,
K
K
K
K
,
Z
ZZ
Z
,
D
D
D
D1
1
1
1
N
N
N
NO
O
O
OT
TT
TE :
E :
E :
E :
Above flow limits are relate d to standard application of
4-way directional control valve using two flow directions,
e.g: P
P
P
P
to A
A
A
A
and simultaneously B
B
B
B
to
T
TT
T
. When 4-way
directional control valve with only one flow direction is
used, e.g. P
P
P
P
to A
A
A
A
(B
B
B
B
plugged) or A
A
A
A
dt T
TT
T
(B
B
B
B
plugged), then
the actual flow limits are considerably lower.
3
0
∆
P
(
M
P
a
)
0,8
1,6
1,8
0,6
1,4
0,4
1,2
0,2
1,0
P A
→
A
T
→
B
T
→
P B
→
B
A
→
300
250
100
50
400
350
450
200
150
Q (dm / min)
1
2
0
∆
P
(
M
P
a
)
0,8
1,6
1,8
0,6
1,4
0,4
1,2
0,2
1,0
P T
→
P A
→
A
T
→
B
T
→
P B
→
300
250
100
50
400
350
450
200
150
Q (dm / min)
3
E
EE
E
, J
J
J
J
, L
L
L
L
, M
M
M
M
, Q
Q
Q
Q
, R
R
R
R
, U
U
U
U
,
F, V
F, V
F, V
F, V
, W
W
W
W
, C
C
C
C
, D
D
D
D
, K
K
K
K
, Z
ZZ
Z
7
21
35
14
28
450
450
370
320
300
360
250
210
180
G
G
G
G
, H
H
H
H
, S
S
S
S
, T
TT
T
, D1
D1
D1
D1
160
3
2
2
2
2-
-
-
- a
aa
and
nd
nd
nd 3
3
3
3- p
- p
- p
- po
o
o
ossssit
it
it
itiiiio
o
o
on
n
n
n
, spri
spri
spri
spring ce
ng ce
ng ce
ng cen
n
n
ntered vers
tered vers
tered vers
tered vers iiiio
o
o
on
n
n
nssss
sp
sp
sp
spo
o
o
oo
o
o
ol type
l type
l type
l type
(diagrams see page 8)
press
press
press
pressure
ure
ure
ure p
p
p
p
[M
M
M
MP
P
P
Pa
aa
a
]
fl
fl
fl
flo
o
o
ow r
w r
w r
w rate Q
ate Q
ate Q
ate Q
[dm
dm
dm
dm
/mi
mi
mi
min
n
n
n
]
C)
o
/s and temperature t = 50
2
ν
= 41 mm
(measured at viscosity
0
∆
P
(
M
P
a
)
0,8
1,6
1,8
0,6
1,4
0,4
1,2
0,2
1,0
P T
→
B
A
→
300
250
100
50
400
350
450
200
150
Q (dm / min)
1
2
3