12
4 Technical Specifications 4
Machine
Heating
P25
Steam
P30
Steam
Other:
Dist. throughput (DIN 11916) max. l/h (US gal/h) 240 (63.4) 240 (63.4)
Filter throughput l/h (US gal/h) 5000 (1320) 5000 (1320)
Filter surface, economy filter m
2
(ft2) 5.0 (53.8) 5.0 (53.8)
Weight without solvent machine
distillation
kg (lb)
kg (lb)
1530 (3373.6)
750 (1653.8)
1560 (3373.6)
750 (1653.8)
Weight with solvent w/o distillation
with distillation
kg (lb)
kg (lb)
2100 (4630.5)
1130 (2491.6)
2130 (4696.6)
1130 (2491.6)
Floor space (with distillation) m
2 (
ft
2
) 5.3 (57.0) 5.3 (57.0)
Floor surface *** m
2
(ft
2
) 1.8 (19.4) 1.8 (19.4)
Cage centrifugal force N (lb) 9400 (2113.1) 11300 (2540.2)
Floor load, stat. and dyn. N/m
2
(lb/ft
2
) 16600 (346.8) 17800 (371.8)
Noise level dB (A) 62 62
Heat balance:
Heat to dissipate
via cooling water ****:
Without Slimsorba kJ/h 52000 53000
With Slimsorba ** kJ/h 53000 54000
Heat dissipated to the surroundings *:
Without Slimsorba kJ/h 15300 16000
With Slimsorba 15500 16200
* Values apply to a standard 2-bath load, 1
st
bath low level for distillation at
cooling water inlet temperature + 12 °C (53.6 °F), cage housing outlet temperature 50 °C (122 °F),
condensation pressure 22 bar (319.1 psi), 16 min. drying,4 min. reduction steam supply 4 - 5 bar
(58 - 72.1 psi) overpressure, saturated steam, ambient temperature 5 to + 40 °C (41 to +95 °F)
** Inc. desorption process per 25 cycles
*** For portion of the floor surface for force transmission, see Installation Instructions, Point 5.3.1
**** Refers to water without any additives
Subject to change!
P25/P30