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Technology for preparing sodium fluorosilicate through fluoride-containing wastewater

A technology of sodium fluorosilicate and fluorosilicic acid, which is applied in the field of photoelectric glass deep processing, can solve the problems of high price, limited resources, unfavorable environmental protection, etc., and achieve the effects of reducing production costs, large particles, large economic benefits and environmental protection benefits

Inactive Publication Date: 2015-12-23
湖南有色氟化学科技发展有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The production of sodium fluorosilicate, in which the source of fluorosilicate mainly comes from fluorite and phosphate rock, with the proven fluorite resources and the continuous consumption of phosphate rock in phosphate and compound fertilizer enterprises, resources are limited, and fluorine resources belong to High-energy-consuming chemical products have high production costs, are expensive, and are not conducive to environmental protection. Therefore, more and more attention has been paid to rational and effective use of fluorine resources in wastewater

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  • Technology for preparing sodium fluorosilicate through fluoride-containing wastewater

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Embodiment 1

[0019] This embodiment includes the following steps:

[0020] (1) Preparation of fluorosilicic acid: add 1000mL fluorine-containing wastewater to a 2L reactor, wherein the molar concentration of fluorine in the fluoride-containing wastewater is 4.983mol / L, and then add silica with a mass fraction of 72% to the fluoride-containing wastewater 129.41g of silicon slag, the molar ratio of fluorine in the fluorine-containing wastewater to silicon in the silicon slag is controlled to be 3.2:1, the reaction temperature is controlled at 10°C, the stirring speed is 350r / min, and the reaction time is 15min. After the reaction is completed, it is filtered to obtain Fluorosilicic acid solution;

[0021] (2) Preparation of sodium fluorosilicate: Add 497 mL of sodium chloride solution with a mass concentration of 20% to the fluorosilicate solution obtained in step (1), and control the molar ratio of sodium chloride and fluorosilicate in the solution to 1.7: 1. Control the reaction temperatu...

Embodiment 2

[0024] This embodiment includes the following steps:

[0025] (1) Preparation of fluorosilicic acid: Add 1000mL fluorine-containing wastewater to a 2L reactor, wherein the molar concentration of fluorine in the fluoride-containing wastewater is 4.983mol / L, and then add silica with a mass fraction of 73% to the fluoride-containing wastewater 116.71g of silicon slag, the molar ratio of fluorine in the fluorine-containing wastewater to silicon in the silicon slag is controlled to be 3.5:1, the reaction temperature is controlled at 20°C, the stirring speed is 380r / min, and the reaction time is 20min. After the reaction is completed, it is filtered to obtain Fluorosilicic acid solution;

[0026] (2) Preparation of sodium fluorosilicate: Add 446mL of sodium chloride solution with a mass concentration of 25% to the fluorosilicate solution obtained in step (1), and control the molar ratio of sodium chloride and fluorosilicate in the solution to 1.9:1 , the reaction temperature is con...

Embodiment 3

[0029] This embodiment includes the following steps:

[0030] (1) Preparation of fluorosilicic acid: Add 1000mL fluorine-containing wastewater to a 2L reactor, wherein the molar concentration of fluorine in the fluoride-containing wastewater is 4.983mol / L, and then add silica with a mass fraction of 73% to the fluoride-containing wastewater 110.40g of silicon slag, the elemental molar ratio of fluorine in the fluorine-containing wastewater to silicon in the silicon slag is controlled to be 3.7:1, the reaction temperature is controlled at 25°C, the stirring speed is 410r / min, and the reaction time is 30min. After the reaction is completed, it is filtered to obtain Fluorosilicic acid solution;

[0031] (2) Preparation of sodium fluorosilicate: add 491 mL of sodium chloride solution with a mass concentration of 25% to the fluorosilicate solution in step (1), and control the molar ratio of sodium chloride and fluorosilicate in the solution to 2.1:1. The reaction temperature is co...

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Abstract

The invention discloses a technology for preparing sodium fluorosilicate through fluoride-containing wastewater. The technology comprises the following steps that 1, silicon slag is added in the fluoride-containing wastewater at 10 DEG C-35 DEG C, the stirring speed is set at 350-450 r / min, the reaction time is set at 15-35 min, and then filtering is performed to obtain a fluosilicic acid solution; 2, a sodium chloride solution is added in the fluosilicic acid solution, the reaction temperature is controlled at 10 DEG C-35 DEG C, the reaction time is controlled to be 20 min 40 min, filtering is performed, and the sodium fluorosilicate product is obtained when a filter cake is dried. According to the technology for preparing the sodium fluorosilicate through the fluoride-containing wastewater, after the industrial fluoride-containing wastewater is treated, the fluorine content in the wastewater is reduced to 0.1 g / L-0.5 g / L, the content of aluminum and boron is not basically changed, the treated wastewater can be recycled through deep fluoride removal, therefore, recycling of fluorine and silicon resources can be achieved, the production cost is lowered, and the better economic benefit and environmental protection benefit are achieved.

Description

technical field [0001] The invention relates to the technical field of photoelectric glass deep processing, in particular to a process for preparing sodium fluorosilicate by utilizing fluorine-containing waste water. Background technique [0002] With the development of my country's economy and the rise of the construction climax, the glass industry has developed rapidly. With the expansion of original film enterprises and the rapid growth of people's market demand for functional glass, the glass deep processing industry has also developed rapidly. In these glass deep-processing enterprises, a large amount of industrial fluorine-containing wastewater will be produced. Enterprises are facing severe environmental protection pressure. How to deal with industrial fluorine-containing wastewater and realize the comprehensive utilization of resources is an urgent problem to be solved. [0003] At present, the main treatment method for the fluorine-containing wastewater in the glass...

Claims

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Application Information

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IPC IPC(8): C01B33/10
Inventor 梁亚娟廖志辉李程文王子龙刘东晓段立山
Owner 湖南有色氟化学科技发展有限公司
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