a
TECHNICAL DATA
TECHNICAL DATA
TECHNICAL DATA
TECHNICAL DATA
TECHNICAL DATA
Refrigerant R407c
Refrigerant R407c
Refrigerant R407c
Refrigerant R407c
Refrigerant R407c
M ODE L KAP P A V 2001
16. 1
18. 1
23. 1
27. 1
32. 2
Co o l in g
(*)
Nominal capacity
kW
155,9
180,2
223,8
269,5
311,7
Water flow evaporator
(1)
l/s
7,447
8,608
10,691
12,878
14,894
l/h
26.810
30.990
38.489
46.360
53.619
Pressure drop evaporator
kPa
39,6
45,2
26,7
38,7
39,6
Heatin g
(**)
Nominal capacity
kW
154,5
178,7
219,5
263,4
309,1
Water flow condenser
(1)
l/s
7,383
8,536
10,487
12,586
14,767
l/h
26.580
30.728
37.753
45.311
53.160
Pressure drop condenser
kPa
38,9
44,5
25,7
37
38,9
Co m p res s o rs
tipo
Number
n
1
1
1
1
2
Absorbed power cooling
(*)
kW
60,1
69,5
83,9
100,1
120,3
Absorbed power heating
(**)
kW
58,4
67,5
81,4
97,1
116,7
Capacity steps
%
0-50-100
0-50-100
0-50-100
0-50-100
0-25-50-
75-100
Co n d en s er co o li n g fan s
type
Total air flow
m
3
/s
10,833
10,833
22,222
20,889
21,111
m
3
/h
39.000
39.000
80.000
75.200
76.000
Fan motor capacity
n x kW
2 x 2,0
2 x 2,0
4 x 2,0
4 x 2,0
4 x 2,0
Nominal fan speed
RPM
Motor power supply
V/Ph/Hz
R efri g eran t ch arg e
Chiller version
kg
1 x 38
1 x 39
1 x 68
1 x 82
2 x 38
Heat pump version
kg
1 x 44,0
1 x 45,0
1 x 81,4
1 x 95
2 x 44,0
O i l
Oil charge
kg
1 x 10
1 x 10
1 x 11
1 x 11
2 x 10
Oil brand
Oil Type
Evap o rato r
type
Evaporator water content
l
1 x 14,3
1 x 15,7
1 x 22,0
1 x 22,0
2 x 14,3
Exchanger max working pressure
water side
bar
30
30
25
25
30
Di men s io n s an d weig h ts
Length
mm
2.649
2.649
2.789
2.789
2.796
Width
mm
1.256
1.256
2.303
2.303
2.280
Height
mm
2.385
2.385
2.385
2.385
2.385
Shipping weight
kg
1.305
1.331
1.842
1.892
2.583
(1) total water flow
(*) outside air temperature 35 °C; water temperature entering/leaving evaporator 12-7 °C.
(**) outside air temperature 8 °C BS, 50% U.R. - water temperature entering/leaving condenser 40-45 °C.
DEA
SE 170
semiermetico a vite
assiali
900
400V 3 ~ 50Hz
scambiatore a piastre
Summary of Contents for KAPPA V 2001
Page 69: ......
