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Method for co-producing dawsonite and tobermorite from fly ash

A technology for hydrating calcium silicate and dawsonite, which is applied in the field of solid waste resource utilization, can solve the problems of low purity of Si/Al separation, low purity of sodium aluminate eluate, and low aluminum-silicon ratio. Low-level problems, to achieve the effect of wide adaptability of raw materials, comprehensive utilization of low cost and high added value, and high activity

Active Publication Date: 2017-03-29
CENT SOUTH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] In order to solve the problems of complex process and low aluminum-silicon ratio of aluminum eluate in the prior art, the present invention provides a method for extracting and co-producing dawsonite and calcium silicate hydrate from fly ash; Improving the separation effect of aluminum / silicon under the premise of shortening the preparation process
In view of this, the present inventor attempts to shorten the process flow on the basis of the prior art, and carry out one-step reaction desiliconization to directly produce calcium silicate hydrate and aluminum products, but it has been difficult to overcome the low separation purity of Si / Al and the low purity of aluminum-silicon. Low ratio and other problems, the purity of the sodium aluminate eluate obtained by the separation of silicon / aluminum is not high

Method used

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  • Method for co-producing dawsonite and tobermorite from fly ash
  • Method for co-producing dawsonite and tobermorite from fly ash
  • Method for co-producing dawsonite and tobermorite from fly ash

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0053] Prepare suspension slurry according to liquid-solid ratio of 10ml / g and calcium-silicon molar ratio of 1.5, add 10g / L sodium hydroxide (based on the slurry) to adjust the pH value of the slurry, stir and mix well and put it into high-pressure reaction In the kettle, hydrothermal reaction was carried out at 240°C and 3.2MPa pressure for 3h. After the reaction is finished, the solid-liquid separation of the reaction product is carried out to obtain the elution liquid and elution slag of aluminum. At a temperature of 35°C, a volume concentration of 30% CO was introduced into the eluate. 2 Gas (CO 2 / N 2 Mixed atmosphere), when the pH value of the solution drops to about 8.5, stop the aeration, and undergo solid-liquid separation to obtain aluminum-containing crystals. The dissolved slag and aluminum-containing crystals were dried at a temperature of 75° C. to constant weight. The dissolved slag and aluminum-containing crystals were weighed to prepare samples, and analy...

Embodiment 2

[0055] Prepare the suspension slurry according to the liquid-solid ratio of 20ml / g and the calcium-silicon molar ratio of 1.2, add 20g / L sodium hydroxide (based on the slurry) to adjust the pH value of the slurry, stir and mix well and put it into the high-pressure reaction In the kettle, hydrothermal reaction was carried out at 220°C and 2.2MPa pressure for 5h. After the reaction is finished, the solid-liquid separation of the reaction product is carried out to obtain the elution liquid and elution slag of aluminum. At a temperature of 55°C, the volume concentration of 50% CO 2 Gas (CO 2 / N 2 mixed atmosphere), when the pH value of the solution drops to about 9.0, stop the aeration, and undergo solid-liquid separation to obtain aluminum-containing crystals. The dissolved slag and aluminum-containing crystals were dried at a temperature of 75° C. to constant weight. The dissolved slag and aluminum-containing crystals were weighed to prepare samples, and analyzed by XRD and...

Embodiment 3

[0057] Prepare the suspension slurry according to the liquid-solid ratio of 30ml / g and the calcium-silicon molar ratio of 1.0, add 40g / L sodium hydroxide (based on the slurry) to adjust the pH value of the slurry, stir and mix well and put it into the high-pressure reaction In the kettle, hydrothermal reaction was carried out at 200°C and 1.8MPa pressure for 7h. After the reaction is finished, the solid-liquid separation of the reaction product is carried out to obtain the elution liquid and elution slag of aluminum. Under the condition of the temperature of 75°C, the eluate was passed through CO with a volume concentration of 70%. 2 Gas (CO 2 / N 2 Mixed atmosphere), when the pH value of the solution drops to about 8.5, stop the aeration, and undergo solid-liquid separation to obtain aluminum-containing crystals. The dissolved slag and aluminum-containing crystals were dried at a temperature of 75° C. to constant weight. The dissolved slag and aluminum-containing crystals ...

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Abstract

The invention provides a method for extracting alumina from fly ash. According to the mol ratio of CaO to SiO2 being 0.3 to 1.5 and the liquid-to-solid ratio being 5ml / g to 50ml / g, quick lime, fly ash and water ingredients are mixed; 5g / L to 100g / L of NaOH is added for regulating the pH value of slurry; the reaction is performed for 0.5h to 12h in a high-pressure sealed container with the temperature being 120 DEG C to 260 DEG C; through solid-liquid separation, digestion solution containing sodium metaaluminate as main ingredients and digestion slag containing tobermorite as main ingredients are obtained; then, CO2 gas with the volume concentration being 10 percent to 100 percent is introduced into the digestion solution; along with the reduction of the pH of the solution, aluminum oxide compounds are separated out in a crystal form; when the pH is 9.5 to 8.0, the gas introduction is completed; then, through the solid-liquid separation operation, crystals containing the dawsonite as the main ingredients are obtained. The method has the advantages that the low-cost recovery and utilization on aluminum resources in the fly ash can be realized; the obtained dawsonite can be used for producing aluminum salt chemical products, or can be used for producing metallurgy grade aluminum oxide and the like after being purified; the obtained tobermorite is used as ingredients for producing cement and concrete, and the product intensity can be improved.

Description

technical field [0001] The invention belongs to the technical field of resource utilization of solid waste, in particular to a method for extracting and co-producing alumina and calcium silicate hydrate from fly ash. Background technique [0002] Fly ash is one of the industrial solid wastes with the largest emissions and stockpiles in the world, and it is also one of the raw materials widely used in cement, building materials, and chemical industries. Dry fly ash is usually gray or off-white, while water-containing fly ash is gray-black, and the main oxide composition is SiO 2 、Al 2 o 3 , Fe 2 o 3 , CaO, MgO, TiO 2 、K 2 O, Na 2 O, MnO, SO 3 etc., where SiO 2 and Al 2 o 3 content of more than 70%. The application of fly ash can be divided into three levels: low, medium and high. The low-level application refers to road construction, soil improvement, mine backfill, etc.; the middle-level application refers to the use as building materials, such as for production ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F7/00C01B33/24
CPCC01B33/24C01F7/00C01P2002/72C01P2006/80
Inventor 李光辉姜涛彭志伟曹鹏旭张元波罗骏张鑫董益佳杨凌志李骞徐斌殷金虎
Owner CENT SOUTH UNIV
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