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Technical Parameters
Model: 2046-2
Processing capacity: 200-220t/h
Vibration power: 2*5.5kw
Pump power: 2*22kw
Concentrator: 400mm*2
Model Technical Parameters
Note: The pump is divided into the vertical pump and horizontal
pump, after treatment, solid particles above 200 mesh and solid
content 70%-80%.
The treatment capacity (treatability) varies according to the solid
content.
Model | Processing capacity (Ton/h) | Vibration power (KW) | Pump power (KW) | Concentrator | Dimensions (L*W*H)(mm) | Theoretical weight (L*W*H)(mm) |
SG90-1 | 50-70 | 2*1.1 | 7.5-11 | 350 | 2840*1270*3016 | 1.5 |
SG90-2 | 70-100 | 2*1.1 | 15 | 250*2 | 2840*1270*3016 | 1.5 |
SG1530-2 | 100-150 | 2*3 | 22 | 300*2 | 3600*1980*3300 | 3.8 |
SG1530-4 | 180-200 | 2*3 | 18.5*2 | 300*4 | 3600*1980*3300 | 4 |
SG1842-2 | 180-200 | 2*3.7 | 18.5*2 | 400*2 | 4800*2274*3750 | 4.5 |
SG1842-4 | 200-280 | 2*3.7 | 22*2 | 350*4 | 4800*2274*3750 | 4.7 |
SG2046-2 | 200-220 | 2*5.5 | 22*2 | 400*2 | 4790*2522*3750 | 5 |
SG2046-4 | 220-320 | 2*5.5 | 22*2 | 350*4 | 4790*2522*3750 | 5.2 |
SG2246-2 | 220-350 | 2*5.5 | 22*2 | 350*4 | 4790*2722*3750 | 6 |
SG2246-4 | 250-380 | 2*5.5 | 30*2 | 400*4 | 4790*2722*3750 | 6.4 |
SG2446-2 | 220-350 | 2*5.5 | 22*2 | 350*4 | 4790*2922*3750 | 6.8 |
SG2446-4 | 250-380 | 2*5.5 | 30*2 | 400*4 | 4790*2922*3750 | 7 |
Operational Principle
A strong centrifugal force is used to separate the mixture under
high-speed rotation.
The classic static hydrocyclone, for example, uses external
pressure to push the feed mixture into the cyclone at a greater
speed, because the mixture moves along the tangential direction of
the cyclone, which causes the liquid to rotate along the wall of
the cylinder. This motion is generally referred to as the outer
swirl.
The particles in the external swirl are subjected to centrifugal
force. If the density of the particle is greater than the density
of the surrounding liquid, it will get more and more centrifugal
force. Once the centrifugal force is greater than the liquid
resistance caused by the movement, the particles will overcome this
resistance and move in the direction of the wall of the device and
separate from the surrounding liquid.
The particles near the wall of the device are driven by the liquid
above the cyclone and move downward along the wall of the cyclone.
The particles near the bottom flow port gather together to form a
suspension with high consistency, which is discharged from the
bottom flow port.
After separation, the liquid rotates downward, and after entering
the cone, the inner diameter of the liquid separator decreases
gradually, and the speed of the liquid rotation accelerates.
Because of the uneven distribution of pressure along the radial
direction when the eddy current is generated, the smaller the axis
is, the closer to the axis it approaches to zero and becomes a
low-pressure region or even a vacuum region, which leads to the
liquid moving towards the axis direction.
The closer to the axis, the smaller the place is.
When arriving at the axis, it approaches to zero becomes a
low-pressure region or even a vacuum region, which causes the
liquid to movetoward the axis.
At the same time, due to the large reduction of the bottom flow
port of the cyclone separator, the liquid cannot be rapidly
discharged from the bottom flow port, and the overflow port in the
center of the top cover of the swirl cavity moves part of the
liquid toward it because it is in the low-pressure area, thus
forming an upward rotational motion and discharging from the
overflow port.