XCF-KYF Integral Unit

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    XCF-KYF Integral Unit

    The XCF flotation machine is used with the KYF flotation machine. The structural features are similar and the dimensions are the same.

    Both XCF and KYF integral unit belong to inflatable flotation machine. With the ability to imbibe ore pulp, SCF is used as ore pulp imbibing tank, while KYF as a direct flow tank without spontaneous imbibition ability. The tanks are arranged horizontally, no foam pump is required.

    U-shaped tank reduces the ore accumulated at the bottom of the tank. Large-diameter conical impeller and short blade rotor are adopted, which enable the machine to possess large processing capacity and low energy consumption. Aeration disperser is arranged in the middle of the impeller, which makes the dispersion of aeration uniform and the mixing sufficient.


    Model

    Effective volume (m³)

    Capacity

    (m³/min)

    Impeller diameter

    (mm)

    Impeller revolutions

    (r.p.m)

    Air pressure of blower

    (Kpa)

    Max of air-infaltion

    (m³/㎡.min)

    Motor power (kw)

    Weight of

    single tank(kg)

    For agitating

    For scraper

    XCF-1

    1

    0.2~1

    400

    358

    ≥12.6

    2

    5.5

    1.1

    1154

    XCF-2

    2

    0.4~2

    470

    331

    ≥14.7

    2

    7.5

    1.1

    1659

    XCF-3

    3

    0.6~3

    540

    266

    ≥19.8

    2

    11

    1.5

    2259

    XCF-4

    4

    1.2~4

    620

    215

    ≥19.8

    2

    15

    1.5

    2669

    XCF-8

    8

    3~8

    720

    185

    ≥21.6

    2

    22

    1.5

    4435

    XCF-16

    16

    4~16

    860

    160

    ≥25.5

    2

    37

    1.5

    6568

    XCF-24

    24

    4~24

    950

    153

    ≥30.4

    2

    37

    1.5

    8000

    XCF-38

    38

    10~38

    1050

    148

    ≥34.3

    2

    75

    1.5

    11000

    Model

    Effective volume (m³)

    Capacity

    (m³/min)

    Impeller diameter

    (mm)

    Impeller revolutions

    (r.p.m)

    Air pressure of blower

    (Kpa)

    Max of air-infaltion

    (m³/㎡.min)

    Motor power (kw)

    Weight of

    single tank(kg)

    For agitating

    For scraper

    KYF-1

    1

    0.2~1

    340

    281

    ≥12.6

    2

    4

    1.1

    826

    KYF-2

    2

    0.4~2

    410

    247

    ≥14.7

    2

    5.5

    1.1

    1419

    KYF-3

    3

    0.6~3

    480

    219

    ≥19.8

    2

    7.5

    1.5

    1885

    KYF-4

    4

    1.2~4

    550

    200

    ≥19.8

    2

    11

    1.5

    2206

    KYF-8

    8

    3~8

    630

    175

    ≥21.6

    2

    15

    1.5

    4190

    KYF-16

    16

    4~16

    740

    160

    ≥25.5

    2

    30

    1.5

    6019

    KYF-24

    24

    4~24

    800

    150

    ≥30.4

    2

    30

    1.5

    7500

    KYF-38

    38

    10~38

    880

    138

    ≥34.3

    2

    55

    1.5

    10300

    KYF (XCF) Type Pneumatic Mechanical Agitating Flotation Machine Structure

    1—impeller 2—air distributor; 3—stator; 4—slot body; 5—spindle; 6—bearing body; 7—Air regulating valve

    The flotation machine uses a "U"-shaped trough body, a hollow shaft inflating and a suspension stator, in particular, a new type of impeller. This is a conical impeller with a blade that is inclined at an angle. It is similar to a high-speed centrifugal pump wheel. It has a large amount of slurry, low heat, low power consumption and simple structure. A porous cylindrical air distributor is also disposed of in the impeller chamber to allow air to be uniformly dispersed in most of the impeller blades in advance, providing a larger slurry-air contact interface.

    During the operation of the flotation machine, as the impeller rotates, the slurry in the tank is sucked from the periphery of the tank from the lower end of the tank to the impeller blade, and at the same time, the low-pressure air fed by the blower passes through the air distributor of the hollow shaft and the impeller. Also entered into it. After the slurry and air are thoroughly mixed between the blades, they are pushed out obliquely from the periphery of the upper half of the impeller, and the stator is stabilized and oriented to enter the entire trough. The bubble rises to the foam stabilization zone, and after the enrichment process, the foam overflows from the overflow weir and enters the foam tank. A part of the slurry flows to the lower part of the impeller and then is stirred by the impeller to remix to form mineralized bubbles, and the remaining slurry flows down to a trough until it finally becomes tailings.

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