Mechanical Specifications And Capacities - VAPORSTREAM VLC Installation Instructions And Maintenance Operations Manual

MECHANICAL SPECIFICATIONS AND CAPACITIES

Table 4-1: Mechanical Specifications and Capacities
S e t a m
c a p a c t i e i s
p r e h o r u
M o d l e
n u m b r e
L b . s K . g
V L C V / L I D 2 1 - 5 7 . 2 6 .
3 1 - 8 6 . 4 0 .
4 1 - 1 1 4 . 5 2 .
5 1 - 1 5 2 . 6 9 .
V L C V / L I D 6 1 - 1 7 1 . 7 8 .
9 1 - 2 5 7 . 1 1 7 .
1 2 1 - 3 4 2 . 1 5 5 .
1 6 1 - 4 5 6 . 2 0 7 .
2 1 1 - 5 9 9 . 2 7 2 .
2 5 1 - 7 1 3 . 3 2 3 .
V L C V / L I D 1 2 2 - 3 4 2 . 1 5 5 .
1 8 2 - 5 1 3 . 2 3 3 .
2 4 2 - 6 8 4 . 3 1 0 .
3 2 2 - 9 1 2 . 4 1 4 .
4 2 2 - 1 1 9 7 . 5 4 3 .
5 0 2 - 1 4 2 5 . 6 4 6 .
V L C V / L I D 1 8 3 - 5 1 3 . 2 3 3 .
2 7 3 - 7 7 0 . 3 5 0 .
3 6 3 - 1 0 2 6 . 4 6 5 .
4 8 3 - 1 3 6 8 . 6 2 1 .
6 3 3 - 1 7 9 6 . 8 1 5 .
7 5 3 - 2 1 3 8 . 9 7 0 .
V L C V / L I D 2 4 4 - 6 8 4 . 3 1 0 .
3 6 4 - 1 0 2 6 . 4 6 5 .
4 8 4 - 1 3 6 8 . 6 2 1 .
6 4 4 - 1 8 2 4 . 8 2 7 .
8 4 4 - 2 3 9 4 . 1 0 8 7 .
1 0 0 4 - 2 8 5 0 . 1 2 9 3 .
* Heater stage identifies the number of contactors.
** Three-phase power supply connection. All heater loads are wired delta.
Capacity Notes
Approximately 172 BTUs (400 kJ) are required to raise the
temperature of one pound (Kg) of water from 40° to 212° F (4°
to 100°C). An additional 970 BTUs (2250 kJ) are required to
change one pound (Kg) of water to water vapor.
The addition of ¾" (25 mm) rigid foil faced fiberglass insula-
tion (optional) on all surfaces of evaporating chamber will
increase unit efficiency by approximately 2%.
4
H e a e t s r
S
Q t . y S a t g e * s 1 2 0 V 2 0 8 V
1 1 1 6 7 . 9 6 .
1 1 2 5 0 . 1 4 4 .
1 1 3 3 3 . 1 9 2 .
1 1 2 5 6 .
3 1 2 8 8 .
3 1 4 3 3 .
3 1
3 1
3 1
3 1
6 2 5 7 7 .
6 2 8 6 5 .
6 2
6 2
6 2
6 2
9 3 8 6 5 .
9 3 1 2 9 8 .
9 3
9 3
9 3
9 3
1 2 4 1 1 5 4 .
1 2 4 1 7 3 1 .
1 2 4
1 2 4
1 2 4
1 2 4
C r u e r t n d a r w a ( m p ) s A (
n i g e l p - h a s e
2 4 0 V 4 8 0 V 6 0 0 V 2 0 8 V
8 3 . 4 2 . 3 3 .
1 2 5 . 6 3 . 5 0 .
1 6 7 . 8 3 . 6 7 .
2 2 2 . 1 1 1 . 8 9 .
2 5 0 . 1 2 5 . 1 0 0 . 1 6 7 .
3 7 5 . 1 8 8 . 1 5 0 . 2 5 0 .
2 5 0 . 2 0 0 . 3 3 3 .
3 3 3 . 2 6 7 . 4 4 4 .
4 3 8 . 3 5 0 .
4 1 7 .
5 0 0 . 2 5 0 . 2 0 0 . 3 3 3 .
7 5 0 . 3 7 5 . 3 0 0 . 5 0 0 .
5 0 0 . 4 0 0 . 6 6 6 .
6 6 7 . 5 3 3 . 8 8 8 .
8 7 5 . 7 0 0 .
8 3 3 .
7 5 0 . 3 7 5 . 3 0 0 . 5 0 0 .
1 1 2 5 . 5 6 3 . 4 5 0 . 7 4 9 .
7 5 0 . 6 0 0 . 9 9 9 .
1 0 0 0 . 8 0 0 . 1 3 3 2 .
1 3 1 3 . 1 0 5 0 .
1 2 5 0 .
1 0 0 0 . 5 0 0 . 4 0 0 . 6 6 6 .
1 5 0 0 . 7 5 0 . 6 0 0 . 9 9 9 .
1 0 0 0 . 8 0 0 . 1 3 3 2 .
1 3 3 3 . 1 0 6 7 . 1 7 7 6 .
1 7 5 0 . 1 4 0 0 .
1 6 6 7 .
Another factor to consider is condensation steam loss from
hoses and tubes. Use the following steam loss guidelines:
• vapor hose: 0.15 lbs/ft/hr (223 g/m/h)
• insulated pipe: 0.05 lbs/ft/hr (74 g/m/h)
• dispersion tubes: 0.5 lbs/ft/hr (744 g/m/h)
)
k W
T h e r e p - h a s e * *
2 4 0 V 4 8 0 V 6 0 0 V
2
3
4
5 3 . 3
1 4 4 . 7 2 . 5 8 . 6
2 1 7 . 1 0 8 . 8 7 . 9
2 8 9 . 1 4 4 . 1 1 5 . 1 2
3 8 5 . 1 9 2 . 1 5 4 . 1 6
2 5 3 . 2 0 2 . 2 1
3 0 1 . 2 4 1 . 2 5
2 8 9 . 1 4 4 . 1 1 5 . 1 2
4 3 3 . 2 1 7 . 1 7 3 . 1 8
5 7 7 . 2 8 9 . 2 3 1 . 2 4
7 7 0 . 3 8 5 . 3 0 8 . 3 2
5 0 5 . 4 0 4 . 4 2
6 0 1 . 4 8 1 . 5 0
4 3 3 . 2 1 7 . 1 7 3 . 1 8
6 5 0 . 3 2 5 . 2 6 0 . 2 7
8 6 6 . 4 3 3 . 3 4 6 . 3 6
1 1 5 5 . 5 7 7 . 4 6 2 . 4 8
7 5 8 . 6 0 6 . 6 3
9 0 2 . 7 2 2 . 7 5
5 7 7 . 2 8 9 . 2 3 1 . 2 4
8 6 6 . 4 3 3 . 3 4 6 . 3 6
1 1 5 5 . 5 7 7 . 4 6 2 . 4 8
1 5 4 0 . 7 7 0 . 6 1 6 . 6 4
1 0 1 0 . 8 0 8 . 8 4
1 2 0 3 . 9 6 2 . 1 0 0