

Add to Cart
Technical Parameters
Model: ZR1500P8L
Belt width: 1500mm
Mud processingcapacity: 15-25t/h
Filter cakeproduction: 4-5t/h
Sediment percentage: 75-85%
Total power: 13kw
Model technical parameters
Model | Belt width (mm) | Mud Processing capacity (Ton/H) | Filter cake production (Ton/H) | Sediment percentage (%) | Total Power of equipment (KW) | Total power (KW) | Dimensions L*W*H(MM) | Weight (KG) |
Zr-1000P8L | 1000 | 10-16 | 2-3 | 75-85 | 3 | 10 | 5500*2000*2100 | 4500 |
Zr-1500P8L | 1500 | 15-25 | 4-5 | 75-85 | 4 | 13 | 5800*2400*2200 | 6500 |
Zr-2000P8L | 2000 | 25-35 | 6-7 | 75-85 | 5.5 | 17 | 7500*2900*2300 | 7600 |
Zr-2500P8L | 2500 | 30-40 | 10 | 75-85 | 5.5 | 17 | 7800*3200*2500 | 9200 |
Zr-3000P8L | 3000 | 40-50 | 12-15 | 75-85 | 11 | 33 | 12500*3500*2500 | 14500 |
Zr-3500P8L | 3500 | 50-60 | 15-17 | 75-85 | 11 | 33 | 13000*14000*2500 | 15500 |
Profile
The structure of the belt type filter press is mainly composed of
transmission device, liquid mix agitator, feeding distributor,
gravity dehydration device, prepress-dewatering porous roller,
high-pressure dewatering roller, alignment extrusion roller,
tensioning device, frame, deviation correcting device, pneumatic
device, filter net, cleaning device, discharging device, bearing
and pedestal, filtrate collecting device, protective device, and centralized electric control cabinet.
Details
1. Transmission device
The transmission device consists of the transmission shaft, sealed
bearing with seat, and cycloidal needle wheel type reducer. The
outer surface of the transmission shaft is coated with high-quality
natural rubber, to increase the friction coefficient of the
transmission. The rotation rate of the motor is controlled by a
frequency converter to ensure the filter belts run stably and the speed is adjustable.
2. Liquid mix agitator
This machine uses a nonblocking static mixer to mix sludge and
chemical liquid (Material that is not easy to be flocculated will
be treated by stirring dynamic mixer). The machine is installed in
front of the sludge distributing flume, and the flocculants come
from surrounding into the sludge tube by high-pressure injection
and then arrive to the mixed reactor. The sludge particles can
collide with diluted polyelectrolyte solution quickly, and the best
flocculation effect and dewatering effect can be achieved by
adjusting the flow rate of sludge and chemical liquid.
3. Feeding distributor
After passing through the flocculating mixer, the sludge enters the
feed distributor. The materials are distributed evenly on the
gravity condensed section by flow guiding, overflow plate, leveling
plate, and the side baffle. In order to improve the gravity
dewatering effect of sludge, a number of water diversion rake teeth
are set above the gravity dewatering area, and the free water from
the upper part of the accumulated sludge is introduced into the
filter net and seep out.
Application