principle
After being heated by clean air, it enters the drying tower and is transformed into tiny droplets using a two fluid (or three fluid) nozzle in the hot air inside the tower. It undergoes rapid heat exchange with the hot air, evaporates the moisture (or solvent) in the liquid material, and is discharged with the hot air to obtain powdered products.
characteristic
1. Especially for high viscosity. Pasty and paste like materials. The effect is excellent and cannot be replaced by other devices.
2. Experimental variety, widely used for low-temperature drying.
3. The nozzle structure is simple, easy to maintain, and has low operating costs.
Technical Parameter
model parameter |
5 |
25 |
50 |
100 |
150 |
200 |
|
evaporation capacity Kg/h |
△t=150℃~90℃ |
1.5 |
7.5 |
15 |
30 |
45 |
60 |
△t=200℃~100℃ |
2.5 |
12.5 |
25 |
50 |
75 |
100 |
|
△t=250℃~90℃ |
3.75 |
18.75 |
37.5 |
75 |
112.5 |
150 |
|
△t=300℃~100℃ |
5 |
25 |
50 |
100 |
150 |
200 |
|
△t=350℃~110℃ |
6 |
30 |
60 |
120 |
200 |
240 |
|
compressed air(m3/min) |
0.9 |
0.9 |
1.1 |
1.5 |
2.7 |
3.4 |
|
Compressed air source(Mpa) |
0.4 |
0.6 |
0.7 |
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Heat source method |
Electricity, electricity+Steam, coal-fired (oil) hot blast stove |
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heating loadKcal/h |
1 |
5 |
10 |
20 |
30 |
40 |
|
fan powerkw |
0.75 |
2.2 |
4 |
7.5 |
11 |
15 |