6 Technical data
It is important to observe the technical data during installation, operation and maintenance. Inform the personnel about
the technical data.
Longstroke
Size
DN/OD
DN
DN/OD
DN
ISO-DIN
51
63.5
76.1 101.6
50
65
80
100
125
150
63.5 76.1
65
80
Air consumption for Balanced Seat-lift
Litre = volume at atmosphere pressure
0.20
0.40
0.40
0.62
0.20
0.40 0.40 0.62
0.62
0.62
0.40
0.40
0.40
0.40
Gallons = volume at atmosphere pressure
0.05
0.11
0.11
0.16
0.05
0.11 0.11 0.16
0.16
0.16
0.11
0.11
0.11
0.11
Air consumption for Tank Seat-lift
Litre = volume at atmosphere pressure
1.10
0.13
0.13
0.21
1.10
0.13 0.13 0.21
0.21
0.21
0.13
0.13
0.13
0.13
Gallons = volume at atmosphere pressure
0.29
0.03
0.03
0.06
0.29
0.03 0.03 0.06
0.06
0.06
0.03
0.03
0.03
0.03
Air consumption for Main Movement
Litre = volume at atmosphere pressure
0.86
1.63
1.63
2.79
0.86
1.62 1.62 2.79
2.79
2.79
1.63
1.63
1.62
1.62
Gallons = volume at atmosphere pressure
0.23
0.43
0.43
0.74
0.23
0.43 0.43 0.74
0.74
0.74
0.43
0.43
0.43
0.43
Kv-value for Balanced CIP Seat-lift [m
3
/h]
1.50
2.50
2.50
1.90
1.50
2.50 2.50 1.90
3.70
3.70
2.50
2.50
2.50
2.50
CV-value for Balanced CIP Seat-lift [GPM]
6.60
11.0
11.0
8.36
6.6
11.0 11.0 8.36
16.3
16.3
11.0
11.0
11.0
11.0
Kv-value for Tank Seat-lift [m
3
/h]
0.90
1.90
1.90
1.40
0.90
1.90 1.90 1.40
3.10
3.10
1.90
1.90
1.90
1.90
CV-value for Balanced Tank Seat-lift [GPM]
3.96
8.36
8.36
6.16
3.96
8.36 8.36 6.16
13.7
13.7
8.36
8.36
8.36
8.36
Kv-value for SpiralClean Spindle CIP [m
3
/h]
0.12
0.12
0.12
0.12
0.12
0.12 0.12 0.12
0.12
0.12
0.12
0.12
0.12
0.12
CV-value for SpiralClean Spindle CIP [GPM]
0.53
0.53
0.53
0.53
0.53
0.53 0.53 0.53
0.53
0.53
0.53
0.53
0.53
0.53
Kv-value for SpiralClean External CIP in
leakage chamber [m
3
/h]
0.25
0.29
0.29
0.29
0.25
0.29 0.29 0.29
0.29
0.29
0.29
0.29
0.29
0.29
CV-value for SpiralClean External CIP in
leakage chamber [GPM]
1.10
1.28
1.28
1.28
1.10
1.28 1.28 1.28
1.28
1.28
1.28
1.28
1.28
1.28
NOTE!
Formula to estimate CIP flow during seat lift (for liquids with comparable viscosity and density to water):
(US measurements)
Q =
Cv •
√ Δ
p
Q =
Cv •
√ Δ
p
Q =
CIP - flow (m
3
/h).
Q =
CIP - flow (gpm)
Kv =
Kv value from the above table
Cv =
Cv value from the above table
Δ
P =
CIP pressure (bar)
Δ
P =
CIP pressure (psi).
Cv =
1.163 x Kv gpm
Cv =
1.163 x Kv gpm
1 bar =
14.5 psi
1 bar =
14.5 psi
Weight (kg)
Longstroke
Size
DN/OD
DN
DN/OD
DN
ISO-DIN
51
63.5
76.1 101.6
50
65
80
100
125
150
63.5 76.1
65
80
Weight (kg)* Unique TO
12.5
22.5
22.5
33
12.5
22.5 22.5
33
36
38
28
28
28
28
Weight (kg)* Unique TO with external cleaning
13
23.5
23.5
34
13
23.5 23.5
34
37
- - -
29
29
29
29
*= without tank flange
35
Содержание Unique TO
Страница 2: ......
