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Characteristics: Feed, filter, rinse, remove residue and regeneration of the filter cloth can be finished sequentially and automatically with high automatization. Wash the materials with multilevel advection or refluence, filter liquid and rinse liquid can be separated. Fast filtration with thin layer can be realized for materials with low filterability and high viscidity. The module design can be consolidated freely with high adaptability. PLC control fits for remote and concentrated control. Snake type deviation correction is adopted to prevent deflection and warp of the filter cloth. |
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Typical Process Drawing: |
| A.Feeding Device H.Vacuum Pump G.Water-return Pump F.Water-expel Separator E.Transfer Valve D.Cloth Washing Device C.Deviation Correction Device B.Rinsing Device |
|
Materials Name |
Liquidtosolid Ratio |
Water Content of Filter % |
Production Efficiency Kg/m3/h |
Materials Name |
Liquidtosolid Ratio |
Water Content of Filter% |
Production EfficiencyKg/m3/h |
|
Citric Acid |
5/1-3/1 |
15 |
25.8 |
Miscible liquids of sodiumhydroxide and CUS |
4/1 |
19.6 |
416 |
|
Zinc Oxide |
10/1 |
51.2 |
75.9 |
ABS resin |
10/1 |
36-38 |
170-232 |
|
Mining slurry soaked by Mno reductico acid |
3.1 |
45.06 |
88.46 |
Calcium Phosphate Ore Magma |
3.5/1 |
21.5 |
345 |
|
Ferromagnet |
2.5/1-4/1 |
7.6 |
500-1000 |
Soluble Phosphor Fertilizer |
2/1-5/1 |
7-10 |
1000-2000 |
|
Sulphur mine |
4/1-2.5/1 |
11.63 |
360-800 |
Vitriol dirt |
1.5/1 |
37-40 |
665-780 |
|
Copper mine |
4/1-2.5/1 |
12 |
400-600 |
Aluminous rocks |
5/1-4/1 |
26.4-29 |
1700 |
|
Mine remaining part |
9/1-4/1 |
21.4 |
300-500 |
Caustic mud |
4/1 |
47-51 |
266-613 |
|
Iron-stone |
2/1-1.5/1 |
8-10 |
2000-3000 |
Residue silicon of aluminium sulphate |
1.5/1 |
37 |
200 |
|
Manganite |
2/1 |
15-17 |
800-1000 |
Fermentated liquid of gentamicin |
1/1-2/1 |
33.1 |
78.5 |
|
Aluminium Hydroxide |
4/1 |
15-17 |
350 |
Coarse zinc oxide |
4/1 |
23.5 |
233 |
|
Fluorite power |
2/1 |
11 |
800 |
Fluoride-bearing calcium lime |
4/1-5/1 |
42-51 |
200-560 |
|
Caustic mud |
4/1 |
47-51 |
266-613 |
Ammonium Salt |
4/1 |
18-20 |
1000-1500 |
|
Vanadium Oxide(V2 O5) |
3/1 |
33 |
174 |
Sodium silicofluoride |
3/1 |
15-20 |
300-500 |
|
Coal ash |
10/1 |
20.7 |
4.9m3/m3/h |
Wet cement |
2/1 |
16-20 |
787 |
|
Gold mine |
2/1 |
25-27 |
111 |
Fine coal of coal dressing |
4/1 |
22.4 |
218 |
|
Sub-ammonium tungstate |
2/1 |
71 |
200 |
Tail coal of coal dressing |
6/1 |
25 |
100 |
|
Organic nitrous dye-stuff |
30/1-20/1 |
69 |
100 |
Zinc Sulfate Ore Magma |
5/1 |
45-50 |
312 |
|
4A zeolite |
80-100 g/L |
≤43 |
164 |
Agate seed |
200-400 g/L |
≤20 |
684 |
|
Finished agate |
260-600 g/L |
≤15 |
125 |
Silica residue |
4.5 |
≤35 |
342 |
|
Baeyer aluminium hydroxide seed |
400-800g/L |
≤15 |
2000 |
Desulfuration Gypsum |
1/1 |
＜10 |
800-1000 |
|
Boehmite |
8/1 |
60 |
30-50 |
|
Filter Width |
0.625-2.0(m) |
2.5-3.0(m) |
0.625m |
1.25 |
1.6 |
2.0 |
2.5 |
3.0 | ||||||||
|
Filter Length |
N | L | N | L |
Filter Area |
Weight |
Filter Area |
Weight |
Filter Area |
Weight |
Filter Area |
Weight |
Filter Area |
Weight |
Filter Area |
Weight |
|
3000 |
0 |
6125 |
1 |
6150 |
1.9 |
2400 |
3.8 |
2850 |
4.8 |
3100 |
6.0 |
3400 |
7.5 |
3800 |
9.0 |
4200 |
|
4500 |
1 |
7625 |
2 |
7650 |
2.8 |
2600 |
5.6 |
3100 |
7.2 |
3400 |
9.0 |
3750 |
11.3 |
4200 |
13.5 |
4650 |
|
6000 |
2 |
9125 |
3 |
9150 |
3.8 |
2800 |
7.5 |
3350 |
9.6 |
3700 |
12.0 |
4100 |
15.0 |
4600 |
18.0 |
5100 |
|
7500 |
3 |
10625 |
4 |
10650 |
4.7 |
3000 |
9.4 |
3600 |
12.0 |
4000 |
15.0 |
4450 |
18.8 |
5000 |
22.5 |
5550 |
|
9000 |
4 |
12125 |
5 |
12150 |
5.6 |
3200 |
11.3 |
3825 |
14.4 |
4300 |
18.0 |
4800 |
22.5 |
5400 |
27.0 |
6000 |
|
10500 |
5 |
13625 |
6 |
13650 |
6.6 |
3400 |
13.1 |
4100 |
16.8 |
4600 |
21.0 |
5150 |
26.3 |
5800 |
31.5 |
6450 |
|
12000 |
6 |
15125 |
7 |
15150 |
7.5 |
3600 |
15.0 |
4350 |
19.2 |
4900 |
24.0 |
5500 |
30.0 |
6200 |
36.0 |
6900 |
|
13500 |
7 |
16625 |
8 |
16650 |
8.4 |
3800 |
16.9 |
4600 |
21.6 |
5200 |
27.0 |
5850 |
33.8 |
6600 |
40.5 |
7350 |
|
A |
600 |
600 |
600 |
600 |
500 |
500 | ||||||||||
|
B |
2400 |
2400 |
2400 |
2400 |
2000 |
2000 | ||||||||||
|
C |
3000 |
3000 |
3000 |
3000 |
2000 |
2000 | ||||||||||
|
D |
1550 |
1550 |
1650 |
1650 |
1700 |
1700 | ||||||||||
|
E |
1100 |
1800 |
2200 |
2600 |
3150 |
3650 | ||||||||||
|
F |
2100 |
2800 |
3200 |
4200 |
4150 |
4650 | ||||||||||
|
G |
973.5 |
973.5 |
973.5 |
973.5 |
1028.5 |
1028.5 | ||||||||||
|
H |
1348.5 |
1348.5 |
1348.5 |
1348.5 |
1403.5 |
1403.5 | ||||||||||
|
I |
585 |
585 |
585 |
585 |
612 |
612 | ||||||||||
|
J |
1104 |
1104 |
1104 |
1104 |
1163 |
1163 | ||||||||||
|
K |
2030 |
2736 |
3136 |
3536 |
4146 |
4646 | ||||||||||
|
M |
1300 |
1300 |
1300 |
1300 |
1300 |
1300 | ||||||||||
|
R |
1250 |
1250 |
1250 |
1250 |
1350 |
1350 | ||||||||||
|
S |
1400 |
2100 |
2500 |
2900 |
3450 |
3950 | ||||||||||
|
T |
1670 |
1670 |
1770 |
1770 |
1870 |
1870 | ||||||||||
|
|
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|
Environmental Protection |
Food |
 |
 |
|
Chemical Industry |
Metallurgy |
|
Chemicals |
Active carbon |
Catalyzer |
Minerals |
Aluminium hydroxide |
Sylyine |
Foods |
Acetic acid |
Fertilizer |
Calcium carbonat |
|
Aluminium fluoride |
Dye and the intermediate |
Mud of coal |
Decomposed of starch |
Calcium sulphate | |||||
|
Gel of alumina |
Industrial scour |
Copper concentrates |
Calcium citrate |
Calcium uitrate | |||||
|
Aluminium hydroxide |
Ferric oxide |
Golden deposite |
Calcium oxalate |
Mud of nitrate-phosphate method | |||||
|
Aluminium phosphate |
Alumina |
Magnese carbonate |
Calcium sulphate |
Environmental protection |
Industrial waste water | ||||
|
Aluminium sulphate |
Lithopone |
Magnesium hydroxide |
Glutamic acid |
Urban sewage | |||||
|
Amino Acid |
Magnesium carbonate |
Magnese carbonate |
Sucrose |
Mire, etc | |||||
|
Barium salt |
Magnesium hydroxide |
Filtered oreremainder |
Citric acid |
||||||
|
Borate |
Nickel salt |
Phosphate |
Lactic acid |
||||||
|
Boracic acid |
Peroxide |
Red mud |
Maltose |
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|
Bromic salt |
Phosphoric acid |
Rutile |
Protein |
||||||
|
Zinc salt |
Dope |
Recovered matter of silver |
Plant oil |
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|
Plasticizer |
Decomposed product of titanium ore |
