Method for production of alumina, joint product of cement and joint product of 4A zeolite molecular sieve with high aluminum fly ash
A high-aluminum fly ash, zeolite molecular sieve technology, applied in alumina/aluminum hydroxide and other directions, can solve the problems of large material consumption, low added value, and high consumption of raw materials, reduce energy consumption and cost, and reduce waste residue discharge. , The effect of reducing material flow
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Embodiment 1
[0052] figure 1 It is the method flowchart of producing alumina, co-production cement and co-production 4A zeolite molecular sieve for embodiment 1 high-alumina fly ash; figure 2 Scanning electron microscope picture of the 4A zeolite molecular sieve prepared in Example 1.
[0053] The method for producing alumina, co-production cement and co-production 4A zeolite molecular sieve with high alumina fly ash in this embodiment comprises the following steps:
[0054] 1) Pre-desiliconization, mix high-alumina fly ash with 15% sodium hydroxide solution at a mass ratio of 0.5:1, pass through a casing heater after mixing and heat to 120°C and import it into a pressure-resistant container Carry out the desiliconization reaction, the reaction time is 2.0h, and then filter to obtain the desiliconization liquid in the liquid phase (used to prepare 4A zeolite molecular sieve after filtering with a leaf filter) and the fly ash filter cake in the solid phase after depressurization from the ...
Embodiment 2
[0067] The method for producing alumina from high alumina fly ash comprises the steps:
[0068] 1) For pre-desilication, mix high-alumina fly ash and 15% sodium hydroxide solution at a mass ratio of 0.5:1, pass it into a casing heater, heat it to 125°C, and import it into a pressure-resistant container Carry out the desiliconization reaction for 1.5 hours, and carry out liquid-solid separation after depressurization from the evaporator to obtain the desiliconization liquid in the liquid phase and the fly ash filter cake in the solid phase, wherein the aluminum-silicon ratio of the original fly ash is 1.12, and after desiliconization raised to 2.08. SiO in desiliconization solution 2 The concentration is 62g / l;
[0069] 2) Preparation of raw slurry: add limestone (quicklime) and sodium carbonate solution to the fly ash filter cake to obtain a mixed slurry, adjust the calcium ratio to 1.96, and the sodium ratio to 1.0, grind the mixed slurry and prepare a raw slurry , the moi...
Embodiment 3
[0078] A method for producing alumina co-production cement with high-alumina fly ash, wherein the steps for producing alumina with high-alumina fly ash are the same as in Example 2.
[0079] The method for aluminum co-production cement comprises: a section of dissolution coarse slag in embodiment 2 step 4) and N 2 o k , N 2 o c 、Al 2 o 3 The second-stage adjustment solution with a concentration of 12g / L, 3g / L, and 13g / L was mixed in a rod mill and reacted while grinding to carry out the second-stage dissolution. The dissolution time was 10min and the dissolution temperature was 78°C. The second-stage dissolution slurry is introduced into the settling tank, diluted with water, and subjected to sedimentation and separation. The bottom flow is the second-stage dissolution residue. The average particle size of the second-stage dissolution residue is between 40 and 70 μm, and the maximum particle size does not exceed 200 μm. The second-stage eluate of the overflow phase is use...
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