Principle
The air stream containing dust passes through low box form air inlet. Parts of it deposit. When light particle dust is floated, it is retarded in the bag. The purified air penetrates the filtrating bag and passes into the up box through Venturi tube and exhausts from outlet.
The accumulated powder dust on the outer wall of filtering bag is increased continuously. If the resistance reaches the limit range(in generally, it should be 80~120mmH2O), it is necessary to clean the accumulated powder dust. The clean method is as follows: controller touches off each control valve in order. It makes the compressed air inside the tand sprays out through nozzles(the 1st wind ,). Using Venturitube, several times of air around it(the 2ndwind )enters into the bag and makes the filtering bag expand rapidly at momentary and accompany and with the counter action of air stream. This makes the dust drop gate and discharge outside the machine.
Technical Parameters:
|
parameter/type
|
MC24
|
MC36
|
MC48
|
MC60
|
MC72
|
MC84
|
MC96
|
MC120
|
|
filtering aream2
|
18
|
27
|
36
|
45
|
54
|
63
|
72
|
90
|
|
filtering bag numberpiece
|
24
|
36
|
48
|
60
|
72
|
84
|
96
|
120
|
|
filtering air speedm/s
|
2-4
|
|
filtering air volumem3/h
|
2160-4300
|
3250-6480
|
4320-8630
|
5400-10800
|
6450-12900
|
7550-155100
|
8650-17300
|
10800-20800
|
|
max overall dimension(mm
|
long
|
1025
|
1425
|
1820
|
2225
|
2625
|
3025
|
3585
|
4385
|
|
wide×high
|
1678×3660
|
|
dust remover
|
pulse #118alue number
|
4
|
6
|
8
|
10
|
12
|
14
|
16
|
20
|
|
compressed air consumptionm3
|
0.07-0.15
|
0.11-0.22
|
0.15-0.30
|
0.18-0.37
|
0.22-0.44
|
0.25-0.50
|
0.29-0.56
|
0.37-0.73
|
|
compressed air pressurekg/cm2
|
5-7≥4
|
