Method for processing spodumene

1. A method for thermally processing α-spodumene by which treatment it is transformed into ρ-spodumene; wherein concentrate or ore with a grain size of 20-1,000 μm is processed in a fluidized bed reactor, at a temperature within a range of 800-1,000° C., by using an oxygenous gas as the fluidizing gas, wherein the temperature within the range 800-1,000° C. is chosen to limit formation of molten phases to less than 15% in the fluidized bed; and wherein such method outputs β-spodumene, discharged gas, and dust, followed by using the thermal energy of the discharged gas to preheat air to be fed into the fluidized bed reactor, wherein at least part of the dust is recovered by a cyclone and a fiber filter and returned to the fluidized bed reactor and wherein the dust obtained from a fluidized bed cooler is combined with the discharged gas.

2. A method according to claim 1 , further comprising the step of feeding oxygenous fluidizing gas into the fluidized bed reactor so that the free-space velocity of gas is 0.3-1 m/s.

3. A method according to claim 1 , wherein the oxygen content of the oxygenous fluidizing gas to be fed in the fluidized bed reactor equals an oxygen quantity required by the oxidation of the fuel needed for heating the fluidized bed.

4. A method according to claim 1 , wherein the fluidized bed is a bubbling bed.

5. A method according to claim 1 , wherein the delay of spodumene in the fluidized bed is no more than one hour.

6. A method according to claim 1 , wherein the discharged gas is utilized in the drying and preheating of a next material to be fed in the fluidized bed reactor.

7. A method according to claim 4 , wherein fuel is fed to the bubbling fluidized bed reactor by lances.

8. A method according to claim 1 , wherein dust is recovered prior to feeding the discharged gas to the fluidized bed reactor.

9. A method of thermally processing α-spodumene into β-spodumene, comprising the steps of:

a. Setting a first processing temperature of a fluidized bed reactor of 800-1,000° C. corresponding to an α-spodumene impurity content;

b. Selecting a quantity of α-spodumene having an active grain size of 20-1,000 μm and an active impurity content;

c. Feeding the selected quantity of α-spodumene into the fluidized bed reactor;

d. Setting a free-space velocity of fluidizing gas fed into the fluidized bed reactor within the range of 0.3-1 m/s;

e. Utilizing the energy content of gas exhausted from the fluidized bed reactor for drying and preheating the α-spodumene; and

f. Recovering dust released with the gas exhausted from the fluidized bed reactor in a cyclone and a fiber filter and returned to the fluidized bed reactor; wherein the dust obtained from a fluidized bed cooler is combined with the discharged gas.