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Method and device for preparing nano silicon dioxide by using silica gel solid waste in high-valued manner

A nano-silica, high-value technology, applied in the direction of silica, silicon oxide, nanotechnology for materials and surface science, etc., can solve the problem of difficult to obtain high-quality nano-silica, silica products Problems such as large particle size, insufficient mixing and reaction, etc., to achieve the effect of easy batch stable production, good industrialization prospects, and enhanced accessibility and reactivity

Active Publication Date: 2022-06-07
BEIJING UNIV OF CHEM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since the alkali hydrolysis of silica gel solid waste and the acidification process of the alkali hydrolysis product silicate are all slow reactions, when carried out in a traditional tank reactor, the silicate and silicic acid generated during the reaction process are easy to coat and deposit. On the surface of silica gel particles, and the large reaction space of the tank reactor is likely to cause uneven local concentration and mass distribution in the reactor, insufficient mixing and reaction, and eventually lead to large particle size, uneven particle size distribution, and Problems such as high impurity content make it difficult to obtain high-quality nano-silica

Method used

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  • Method and device for preparing nano silicon dioxide by using silica gel solid waste in high-valued manner
  • Method and device for preparing nano silicon dioxide by using silica gel solid waste in high-valued manner
  • Method and device for preparing nano silicon dioxide by using silica gel solid waste in high-valued manner

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0077] A. Disperse 40 g of silica gel solid waste in 22 mL of deionized water to form a stable suspension, and the mass percentage of silica gel solid waste in the suspension is 19.28%.

[0078] B. Weigh 15.9137 g of sodium hydroxide and dissolve it in 50 mL of deionized water to form a sodium hydroxide solution, and the mass percentage of sodium hydroxide in the sodium hydroxide solution is 24.14%.

[0079] C, the suspension liquid obtained in step A and the sodium hydroxide solution obtained in step B are simultaneously added into the multistage confinement rotary mixing reaction device, the silica in the suspension liquid and the potassium hydroxide in the sodium hydroxide solution are The mass ratio is 1:2, the number of rotor stages is set to 1, the distance between the stator and the rotor is 2mm, the distance between the fine grinding rotor and the stator is 1mm, the rotor speed of the reactor is 4000rad / min, rotate for 30min, and remove the insoluble by filtration. The...

Embodiment 2

[0085] A. Disperse 40 g of silica gel solid waste in 22 mL of deionized water to form a stable suspension, and the mass percentage of silica gel solid waste in the suspension is 19.28%.

[0086] B. Weigh 22.3212 g of potassium hydroxide and dissolve it in 50 mL of deionized water to form a potassium hydroxide solution, and the mass percentage of potassium hydroxide in the potassium hydroxide solution is 30.86%.

[0087] C, the suspension liquid obtained in step A and the potassium hydroxide solution obtained in step B are synchronously added into the multistage confinement rotary mixing reaction device, the silica in the suspension liquid and the potassium hydroxide solution in the sodium hydroxide solution are The mass ratio is 1:2, the number of rotor stages is set to 1, the distance between the stator and the rotor is 2mm, the distance between the fine grinding rotor and the stator is 1mm, the rotor speed of the reactor is 4000rad / min, rotate for 30min, and remove the insolu...

Embodiment 3

[0093] A. Disperse 40 g of silica gel solid waste in 22 mL of deionized water to form a stable suspension, and the mass percentage of silica gel solid waste in the suspension is 19.28%.

[0094] B. Weigh 15.9137 g of sodium hydroxide and dissolve it in 50 mL of deionized water to form a sodium hydroxide solution, and the mass percentage of sodium hydroxide in the sodium hydroxide solution is 24.14%.

[0095] C, the suspension liquid obtained in step A and the sodium hydroxide solution obtained in step B are synchronously added to the multistage confinement rotary mixing reaction device, the silicon dioxide in the suspension liquid and the hydroxide solution in the sodium hydroxide solution The substance mass ratio of potassium is 1:2, the number of rotor stages is set to 2, the distance between the stator and rotor is 2mm, the distance between the fine grinding rotor and the stator is 1mm, the rotor speed of the reactor is 6000rad / min, and the rotation speed is 30min. The inso...

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Abstract

The invention discloses a method and a device for preparing nano silicon dioxide by using silica gel solid waste in a high-valued manner. The preparation method comprises the following steps: (1) preparing a reaction solution; (2) alkaline hydrolysis reaction; (3) carrying out double hydrolysis reaction; (IV) roasting treatment; the device comprises a shell, a stator fixed in the shell and a rotor engaged with the stator, and a fine grinding rotor is arranged at the lower end of the rotating shaft and is connected with a driving shaft of the driving mechanism. The method is simple to operate, short in technological process and easy for batch stable production; meanwhile, the equipment is simple, the cost for preparing the nano silicon dioxide is low, the energy consumption is low, the industrial prospect is better, and an important way is provided for preparing the nano silicon dioxide through high-valued conversion of the silica gel solid waste.

Description

technical field [0001] The invention belongs to the field of silicon dioxide preparation, and in particular relates to a high-value method and device for preparing nano-silicon dioxide by using silica gel solid waste. Background technique [0002] Phosphate resources in my country are often accompanied by 3% to 4% of fluorine, and a large amount of fluorosilicic acid will be by-produced in the production process of wet-process phosphoric acid and phosphate fertilizer. %. Most of the major domestic phosphorus chemical companies realize the comprehensive utilization of fluorine resources by converting the fluorosilicic acid by-product of phosphate fertilizers into hydrogen fluoride or potassium fluoride. [0003] Taking the preparation of potassium fluoride as an example, there are two main ways to produce potassium fluoride by using fluorosilicic acid as the fluorine source: one is that fluorosilicic acid reacts with potassium chloride to obtain potassium fluorosilicate, whic...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B33/18B01J19/18B02C2/10B82Y30/00B82Y40/00
CPCC01B33/18B01J19/18B02C2/10B82Y30/00B82Y40/00C01P2002/72C01P2004/03C01P2006/17C01P2006/12C01P2004/62C01P2004/32C01P2004/64Y02P20/10
Inventor 范国利刘美李峰
Owner BEIJING UNIV OF CHEM TECH
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