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Method for recycling organic silicon slurry

A technology of organosilicon slurry and low boiling matter, which is applied in the field of recycling of organosilicon slurry, can solve problems such as impossibility and complex components, and achieve the effects of reducing pollution, good hydrophobicity, and prolonging the life of buildings

Active Publication Date: 2016-03-30
南通安广美术图案设计有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] With the rapid development of the organosilicon industry, the output of organosilane chlorosilane monomers is also increasing. Organosilicon high boilers are one of the by-products of the production of organosilyl chlorosilane monomers. There are two main sources: one is through refining Distillation of organosilane chlorosilane monomer, this type of high boiling matter accounts for about 5% of chlorosilane monomer, it is easier to carry out industrial development and utilization; the other is derived from organosilicon slurry, this type of high boiling matter accounts for about 5% of monomer About 3% to 5% of the production capacity, the composition is complex, and contains a large amount of solid particles such as silicon and copper, which is easy to react with moisture in the air to form corrosive hydrogen chloride gas, which cannot be treated by simple methods

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] Embodiment 1: a kind of recycling method of organic silicon slag, comprises the following steps:

[0018] (1) adding 23% low boilers to the organic silicon slurry for hydrolysis, the low boilers being any one of methyl chloride, tetramethyl silicon or trichlorosilane or any combination of two or more, During hydrolysis, the temperature is controlled at 45°C, and the hydrolysis is carried out with a low-speed mixer at 20r / min for 3 hours. The hydrolyzed product is subjected to solid-liquid separation with a solid-liquid separator to obtain a supernatant and a precipitate. The supernatant is obtained from the solid-liquid separator. The upper end flows out, and the sediment is discharged from the bottom end of the solid-liquid separator;

[0019] (2) the separated supernatant is carried out alcoholysis with ethanol, the concentration of said ethanol is 50%, the ethanol consumption is 30% of the supernatant, the alcoholysis temperature is 40 ℃, and the alcoholysis time is ...

Embodiment 2

[0023] Embodiment 2: a kind of recycling method of organic silicon slag, comprises the following steps:

[0024] (1) Adding 35.5% low boilers to the organic silicon slurry for hydrolysis, the low boilers being any one or any combination of two or more of methyl chloride, tetramethyl silicon or trichlorosilane, During hydrolysis, the temperature was controlled at 46°C, and the hydrolyzed product was stirred and hydrolyzed with a low-speed mixer at 25r / min for 5 hours. The upper end flows out, and the sediment is discharged from the bottom end of the solid-liquid separator;

[0025] (2) the separated supernatant is alcoholysed with ethanol, the concentration of ethanol is 57.5%, the ethanol consumption is 35% of the supernatant, the alcoholysis temperature is 42.5°C, and the alcoholysis time is 0.75h. Ethanol can dissolve part of the insoluble silanol into ethanol to adjust the content of sodium methyl silicate; the sediment at the bottom is alkalinely hydrolyzed with lye, and ...

Embodiment 3

[0029] Embodiment 3: a kind of recycling method of organosilicon slurry, comprises the following steps:

[0030] (1) adding 48% of low boilers to the organic silicon slurry for hydrolysis, the low boilers being any one or any combination of two or more of methyl chloride, tetramethyl silicon or trichlorosilane, During hydrolysis, the temperature is controlled at 47°C, and the hydrolysis is stirred with a low-speed mixer at 30r / min for 7 hours. The hydrolyzed product is separated from the solid and liquid by a solid-liquid separator to obtain a supernatant and a precipitate. The supernatant is obtained from the solid-liquid separator. The upper end flows out, and the sediment is discharged from the bottom end of the solid-liquid separator;

[0031] (2) The separated supernatant is alcoholysed with ethanol, the concentration of ethanol is 65%, the amount of ethanol is 40% of the supernatant, the alcoholysis temperature is 45°C, the alcoholysis time is 1h, and the alcoholysis tim...

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Abstract

The invention discloses a method for recycling organic silicon slurry, and belongs to the technical field of environment protection. The method comprises the following steps: (1) adding a low-boiling-point substance in organic silicon residue slurry for hydrating, and then carrying out solid-liquid separation to obtain supernate and precipitate; (2) performing alcoholysis on the supernate with ethanol, and performing alkaline hydrolysis on the precipitate with an alkaline liquor; (3) completely introducing final products obtained in alcoholysis and alkaline hydrolysis, washing with a potassium chloride solution to obtain diluent and dried residues; (4) mixing the dried residues and cement with sands, mixing with the diluent, and adding water to prepare cement mortar for construction; and (5) mixing the diluent with an organic solvent, adding fatty acid to react, adding water into the reacting product to prepare a construction material water-proofing agent. The method for recycling organic silicon slurry is simple and feasible, the hydrolyzed and dried residues are used for preparing cement mortar, and the diluent can be used for preparing the construction material water-proofing agent, so that waste recycling can be realized, environmental pollution can be reduced, and the requirement for sustained development strategy can be met.

Description

technical field [0001] The invention belongs to the technical field of environmental protection, in particular to a method for recycling organic silicon slag. Background technique [0002] In recent years, with the development of the economy, the acceleration of the industrialization process and the improvement of the level of urbanization, human beings are facing increasing environmental pressure. Waste has always plagued the living environment of residents and disrupted the ecological balance. [0003] Among them, organosilicon slag is a kind of waste with serious pollution. It is a waste slag generated during the synthesis of organosilicon monomer, which accounts for about 3% of the monomer. With the rapid expansion of organosilicon monomer production , accompanied by a large amount of organic silicon waste slurry, its main composition is silicon powder (particle size 2 ~ 150um) brought out by more high boiling matter and a small amount of fluidized bed, copper powder an...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C04B28/00C04B18/04C04B24/08C04B111/27C04B103/65
CPCY02W30/91C04B28/00C04B18/04C04B24/08C04B2103/65C04B2111/27C04B14/06
Inventor 卢连伟
Owner 南通安广美术图案设计有限公司
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