A continuous calcination system and method for pearlescent materials
A pearlescent material and calcination technology, which is applied in the direction of chemical instruments and methods, fibrous fillers, inorganic pigment treatment, etc., can solve the unstable quality control of pearlescent material calcination, unfavorable calcining of pearlescent material with small batch color number, and affect the quality of pearlescent material products and other problems, to achieve good calcination effect, realize energy consumption calcination, and shorten calcination time
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Embodiment 1
[0031] Such as figure 1 As shown, a system for the continuous calcination process of pearlescent materials, the system includes a raw material bin 1 connected in sequence, a screw feeder 2, a feed valve 3, a fluidized bed reactor 4, a main heating furnace 5, and a primary cyclone separation Device 6, secondary cyclone separator 6-1, one-point return valve 7, two-point return valve 8, metal dust collector 9, induced draft fan 10, chimney 11, discharge valve 12, water-cooled screw 13, product silo 14 , gas heat exchanger 15, gas heating electric furnace 16, air blower 17, water pump 18 and cooling tower 19;
[0032]In the system, the outlet of the raw material bin 1 is connected to the screw feeder 2, the outlet of the screw feeder 2 is connected to the inlet of the feed valve 3, and the outlet of the feed valve 3 is connected to the fluidized bed The feed port of the reactor 4 is connected, the gas inlet of the fluidized bed reactor 4 is connected with the gas outlet of the ga...
Embodiment 2
[0036] A method for continuous calcination of pearlescent materials based on the system described in Example 1, the method for continuous calcination of pearlescent materials comprises the following steps:
[0037] 1) The pearlescent material precursor powder enters the fluidized bed reactor 4 through the raw material bin 1 through the screw feeder 2 through the feed valve 3; Coarse particles, after being collected by the primary cyclone separator 6 and the secondary cyclone separator 6-1, enter the fluidized bed reactor 4 through the one-point return valve 7 and the two-point return valve 8; the two-stage cyclone separator 6- 1. The finer particle powder entrained in the discharged high-temperature flue gas is collected by the high-temperature metal dust collector 9 and then stored. The purified high-temperature dust-containing gas passes through the induced draft fan 10 and is discharged from the chimney 11; the fully calcined pearlescent material Discharge from the outlet o...
Embodiment 3
[0043] Using the method described in Example 2, the silver-white series pearlescent material precursor powder with a water content of 5% enters the fluidized bed reactor 4 through the feed valve 3 through the raw material bin 1 through the screw feeder 2; the air is heated by the gas The gas heat exchanger 15 heated by the electric furnace 16 enters the fluidized bed reactor 4 to fluidize and calcine the pearlescent material precursor powder in the fluidized bed reactor 4, the calcination temperature is 550° C., and the calcination time is 60 minutes; The first-stage cyclone separator 6 and the second-stage cyclone separator 6-1 enter the metal dust collector 9 for purification, and the purified low-temperature flue gas passes through the induced draft fan 10 and is discharged from the chimney 11; the cooling water of the process water main pipe is pressurized by the water pump 18 , into the water inlet of the water-cooled screw 13 to exchange heat with the hot material, and th...
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