Production of molybdenum powder

    Calcined ammonium paramolybdate or MoO 3 was formed by preparing a raw material powder of molybdenum metal. In industrial production, pure ammonium molybdate can be reduced directly into metal molybdenum powder in a hydrogen furnace, or it can be calcined to MoO 3 at a temperature of 550 to 650 ° C, and then reduced to metal molybdenum powder.
    In the production of molybdenum products by powder metallurgy, molybdenum powder is required to have high purity, low oxygen content, and fine and uniform particle size. Production of molybdenum powder in tube or muffle furnace or kiln with hydrogen back through the secondary reduction of ammonium paramolybdate or MoO 3 is reduced to MoO 2, the second reduction at higher temperatures, the MoO 2 Reduced to metal molybdenum powder. The various reduction process parameters are listed in Tables 1 and 2. At present, some manufacturers use the direct hydrogen reduction method of ammonium paramolybdate to reduce the calcination process and avoid the impurities brought in by calcination. In order to ensure the quality of molybdenum powder, in addition to the reduction temperature, the flow rate and humidity of hydrogen, the thickness and pushing speed of the layer, and the particle size of the raw materials are all factors that affect the particle size of the molybdenum powder. Usually, the H 2 flow rate is large, and the powder having a low dew point reduction is fine, whereas the powder is coarse. Therefore, these factors must be strictly controlled in the production process to obtain a qualified powder.

      Table 1 Main parameters of primary reduction of ammonium paramolybdate

    Equipment

    Feeding amount kg/h  

    Hydrogen flow rate m 3 /h

    Furnace tube inclination (o)  

    Each belt temperature, °C

    1

    2

    3

    4

    5

    Rotary furnace φ400/384mm

    60 to 80

    20 to 30  

    3 to 5  

    360 ~ 380

    420 ~ 440

    500 ~ 540

    550 to 580

    550 to 580

    Four tube muffle furnace 260*60mm  

    5kg / boat / 60min

    7m 3 /h·tube

     

    440

    440

    500

    500

    440

    Table 2 Reduction process parameters of molybdenum in tubular furnace  

    Reduction phase

    equipment

    Boat size mm

    Loading amount g/boat

    Push speed min/boat

    hydrogen

    Furnace temperature in each zone, °C

    Flow rate m 3 /h  

    Dew point °C

    1

    2

    3

    4

    5

    The first stage

    4-tube furnace

    300*60*65

    250 to 280  

    20

    0.2 to 0.3

    < -10  

     

    500 to 550

     

     

    11 tube furnace

    250*40*35  

    150 to 180

    20

     

    < -10  

    350

    450

    520

    540

    520

    second stage

    11 tube furnace

    250*40*35  

    200 to 220

    15

     

     

    850

    920

    920

    920

    880

    13 tube furnace

    250*40*35  

    250

    20

    0.8 to 1.0

    < -10  

    750

    850

    920

    920

    880

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