1 .. 6 7 8 9 10 11 12 13 14 15 16 .. 32
11
Air cooled chillers
LX
PROPELLER
F
ANS
A I R  C O N D I T I O N I N G  -  R E F R I G E R A T I O N  -  A I R  H A N D L I N G  -  H E A T  E X C H A N G E -
N
N
A
A
 
 
0
0
4
4
.
.
5
5
3
3
1
1
 
 
B
B
P
ERFORMANCES
POWERCIA
T LX-LXH-LXC
ST
ANDARD version
Pf :
Cooling capacity calculated with :
Glycol water is necessary
- water inlet/outlet differential as per curves page 16
Low temperature option necessary (valid only on LX versions).
- 0.00005 m2 °C/W fouling factor
EUROVENT conditions
Pa :
Compressors + fans absorbed power
R407C
LX
LXH
LXC
CONDENSER AIR INLET TEMPERA
TURE °C
Evaporator
water oultet
temperature °C
26
29
32
35
38
41
Pf
Pa
Pf
Pa
Pf
Pa
Pf
Pa
Pf
Pa
Pf
Pa
kW
kW
kW
kW
kW
kW
kW
kW
kW
kW
kW
kW
3050 Z
Glycol water
-8
448.7
205.1
429.7
215.5
421.4
228.0
402.0
241.0
383.0
255.3
-6
478.5
208.3
466.5
219.7
450.0
231.7
437.8
245.0
424.8
260.0
-4
513.4
211.9
502.3
223.8
491.8
237.0
471.0
249.7
457.1
264.4
-2
575.9
218.3
559.2
230.4
547.0
243.8
526.2
257.0
513.8
270.2
501.4
288.0
0
619.8
223.2
601.4
235.2
585.0
248.6
572.3
262.5
549.9
276.4
531.5
294.1
2
658.2
227.1
642.7
240.1
626.7
254.0
606.9
267.9
587.9
281.8
574.2
301.2
Pure water
5
753.9
237.9
733.2
251.2
718.3
266.3
695.1
280.8
680.1
297.9
643.8
317.3
6
771.6
240.1
758.2
253.4
739.2
269.0
719.1
284.5
699.5
301.1
678.5
321.3
7
796.7
243.1
778.9
256.4
761.8
272.0
740.2
287.5
717.6
303.9
698.3
324.2
8
819.4
245.9
797.8
259.2
782.9
274.9
762.3
290.7
740.1
307.5
719.9
327.5
10
875.1
260.0
857.7
271.2
837.6
282.4
816.4
298.6
794.2
316.2
773.3
336.0
12
921.6
265.6
906.1
277.2
884.5
288.8
862.9
305.3
841.7
321.7
3400 Z
Glycol water
-8
498.6
225.1
485.3
240.1
468.0
250.0
445.7
263.4
427.0
289.0
-6
534.7
229.8
523.1
242.6
504.0
255.4
484.9
269.5
462.6
293.5
-4
576.3
234.5
561.4
247.4
543.3
260.9
522.7
275.0
504.0
290.4
-2
645.3
242.3
625.3
255.4
612.5
270.6
586.6
284.5
564.9
300.0
542.0
314.2
0
687.6
247.2
671.1
261.2
651.4
275.8
630.6
291.0
611.8
306.0
583.8
320.3
2
735.0
252.7
724.9
268.2
698.4
282.4
672.9
303.8
661.4
313.5
632.6
327.6
Pure water
5
833.8
263.8
814.0
279.9
793.9
295.9
776.0
313.5
746.1
330.0
725.1
342.5
6
858.7
267.8
838.7
283.3
814.1
305.8
795.8
316.7
773.5
334.6
748.2
350.0
7
884.0
271.1
865.0
286.9
844.0
311.7
819.9
320.5
793.9
338.2
770.3
356.5
8
907.2
276.4
890.2
290.3
868.2
315.4
844.5
324.4
819.1
342.6
800.3
363.4
10
971.7
285.0
948.3
308.3
929.8
324.1
903.9
333.7
877.8
352.8
856.2
373.5
12
1026.3
295.7
1000.5
314.6
981.0
333.5
952.7
343.3
928.3
361.4
3750 Z
Glycol water
-8
557.8
245.0
544.0
260.0
518.0
272.1
493.9
286.8
475.0
307.0
-6
593.8
250.9
580.1
265.8
555.3
278.1
536.7
293.6
515.0
311.0
-4
641.4
256.7
624.1
270.8
601.5
284.9
577.5
300.0
553.6
316.1
-2
715.8
265.6
696.1
280.3
675.6
295.7
648.5
317.3
623.4
335.6
594
351.6
0
764.4
271.4
743.9
286.5
724.5
302.8
697.9
325.8
672.6
344.1
643.0
359.8
2
815.3
277.6
801.9
294.4
773.4
310.0
750.3
335.2
717.6
352.7
693.1
361.9
Pure water
5
921.5
291.0
898.0
313.2
874.0
333.8
844.5
352.9
828.1
370.2
788.8
378.9
6
948.3
294.4
924.4
319.5
904.6
338.8
872.3
356.6
850.1
374.2
816.8
383.9
7
976.3
298.0
955.3
323.5
929.5
343.0
902.6
362.2
878.4
379.0
842.8
387.2
8
1005.4
301.9
981.4
328.7
949.8
347.1
929.8
367.0
900.5
383.4
870.5
391.0
10
1069.0
320.2
1045.5
338.6
1019.6
358.2
995.8
377.6
967.0
392.0
943.7
402.5
12
1132.1
330.8
1102.6
347.4
1077.3
367.3
1047.8
388.0
1020.5
411.1
N
OTES
 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .