Method for producing aluminum oxide by Bayer process
A technology of alumina and Bayer method, which is applied in the direction of alumina/hydroxide, etc., can solve the problems of difficult unloading, frequent brushing, and hard filter cake of leaf filter, so as to maintain high-quality operation, reduce power consumption and evaporation The effect of improving steam consumption and production capacity
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Embodiment 1
[0021] Qualified ore slurry liquid phase composition of diaspore type bauxite: total alkali: 127.4g / l alumina: 29.6g / l caustic alkali: 98.0g / l solid content 792g / l solid phase composition: alumina: 58.60 % Silica: 7.73%
[0022] Circulating lye composition: total alkali: 265.0g / l alumina: 125.98g / l caustic: 234.0g / l Rp: 0.538
[0023] Dissolve the qualified slurry of circulating lye and diaspore bauxite according to the ratio of 2.90. After the diaspore bauxite is dissolved, the slurry (that is, before adding diaspore bauxite ) Composition: Alkali: 227.0g / l Alumina: 211.51g / l Caustic: 198.0g / l Rp: 1.068
[0024] Qualified slurry liquid phase composition of gibbsite type bauxite: total alkali: 144.20g / l alumina: 78.29g / l caustic alkali: 125g / l solid content 618g / l solid phase composition: alumina: 47.20% oxide Silicon: 10.37%
[0025] The qualified pulp of gibbsite-type bauxite is added to the stripping and flashing process at full load at a flow rate of 80m3 per hour. The l...
Embodiment 2
[0028] Qualified ore slurry liquid phase composition of diaspore type bauxite: total alkali: 143.2g / l alumina: 45.4g / l caustic alkali: 106.0g / l solid content 762g / l solid phase composition: alumina: 59.40 % Silica: 7.80%
[0029] Circulating lye composition: total alkali: 264.8g / l alumina: 122.36g / l caustic: 230.0g / l Rp: 0.532
[0030]Dissolve the qualified slurry of circulating lye and diaspore bauxite at a ratio of 2.91. After the diaspore bauxite is dissolved, the slurry (that is, before adding diaspore bauxite ) Composition: Alkali: 224.2g / l Alumina: 203.61g / l Caustic: 192.0g / l Rp: 1.060
[0031] Qualified slurry liquid phase composition of gibbsite type bauxite: total alkali: 163.2g / l alumina: 86.18g / l caustic alkali: 132.0g / l solid content 593g / l solid phase composition: alumina: 47.20% Silicon oxide: 15.30%
[0032] The qualified pulp of gibbsite-type bauxite is added to the stripping and flashing process at full load at a flow rate of 90m3 per hour. The liquid phase...
Embodiment 3
[0035] Qualified ore slurry liquid phase composition of diaspore type bauxite: total alkali: 126.8g / l alumina: 32.89g / l caustic alkali: 93.0g / l solid content 804g / l solid phase composition: alumina: 59.70 % Silica: 7.49%
[0036] Circulating lye composition: total alkali: 273.1g / l alumina: 125.16g / l caustic: 235.0g / l Rp: 0.533
[0037] Dissolve the qualified slurry of circulating lye and diaspore bauxite according to the ratio of 2.86. After the diaspore bauxite is dissolved, the slurry (that is, before adding diaspore bauxite ) Composition: Alkali: 225.0g / l Alumina: 208.88g / l Caustic: 191.0g / l Rp: 1.094
[0038] Qualified slurry liquid phase composition of gibbsite type bauxite: total alkali: 151.6g / l alumina: 84.21g / l caustic alkali: 126.0g / l solid content 612g / l solid phase composition: alumina: 47.60% Silicon oxide: 15.46%
[0039] The qualified pulp of gibbsite-type bauxite is added to the stripping and flashing process at full load at a flow rate of 86m3 per hour. The...
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