Process for producing precipitated white carbon black by silicon tetrachloride

A technology for precipitating white carbon black and silicon tetrachloride, applied in the direction of silicon oxide, silicon dioxide, etc., can solve the problems of ineffective treatment, waste of environment, high cost, simple production equipment and process control, and small investment scale , the effect of reducing processing costs

Inactive Publication Date: 2010-06-16
昊华宇航化工有限责任公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The silicon tetrachloride used in gas phase production of white carbon black mostly originates from the silicon tetrachloride by-product of trichlorosilane and polysilicon industry, but there are following problems: 1) the by-product of trichlorosilane and polysilicon industry is tetrachloride The amount of silicon is large, and the ability to produce white carbon black by the gas phase method is limited, so it cannot be processed effectively; 2) The process of producing white carbon black by the gas phase method is complicated and the cost is high, and at the same time, a large amount of low-purity hydrogen chloride by-product can only be made into waste hydrochloric acid , resulting in greater waste and environmental pollution; 3) The fumed silica is expensive, the scope of use is narrow, and the market capacity is small. Carbon black is cheap and widely used, and its market capacity is dozens of times that of fumed silica

Method used

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  • Process for producing precipitated white carbon black by silicon tetrachloride

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] Add 60L of hydrochloric acid solution with a mass concentration of 29% in the reaction kettle, add 3.6g of sodium dodecylbenzenesulfonate dispersant, stir well, and heat through steam in the jacket, and the temperature is controlled at 40°C. Slowly add silicon tetrachloride into the reaction kettle, and control the flow rate of silicon tetrachloride at 0.8m 3 / h, adjust the amount of cooling water at any time during the addition process, and control the temperature in the kettle at 41-45°C. After the hydrogen chloride gas produced in the reaction is treated by filtration, adsorption, separation and other devices, the qualified hydrogen chloride is sent to the PVC or trichlorosilane production device for use, and the unqualified hydrogen chloride is absorbed by water and then replenished to the mother liquid storage tank; continuous sampling during the reaction process Analyze the purity of hydrogen chloride, when the hydrogen chloride purity ≥ 95%, it can all be recover...

Embodiment 2

[0017] Add 60L of hydrochloric acid solution with a mass concentration of 31% in the reaction kettle, add 4.8g of hexadecyltrimethylammonium bromide dispersant, stir well, pass steam into the jacket for heating, and control the temperature at 38°C . Slowly add silicon tetrachloride into the reactor, and control the flow rate of silicon tetrachloride at 1.0m 3 / h, adjust the amount of cooling water at any time during the addition process, and control the temperature in the kettle at 36-40°C. After the hydrogen chloride gas produced in the reaction is treated by filtration, adsorption, separation and other devices, the qualified hydrogen chloride is sent to the PVC or trichlorosilane production device for use, and the unqualified hydrogen chloride is absorbed by water and then replenished to the mother liquid storage tank; continuous sampling during the reaction process Analyze the purity of hydrogen chloride, when the hydrogen chloride purity ≥ 95%, it can all be recovered, an...

Embodiment 3

[0019] Add 60L of hydrochloric acid solution with a mass concentration of 33% in the reaction kettle, add 7.2g of cetyltrimethylammonium bromide dispersant, stir well, pass steam into the jacket for heating, and control the temperature at 32°C . Slowly add silicon tetrachloride into the reactor, control the flow of silicon tetrachloride at 1.2m 3 / h, adjust the amount of cooling water at any time during the addition process, and control the temperature in the kettle at 28-34°C. After the hydrogen chloride gas produced in the reaction is treated by filtration, adsorption, separation and other devices, the qualified hydrogen chloride is sent to the PVC or trichlorosilane production device for use, and the unqualified hydrogen chloride is absorbed by water and then replenished to the mother liquid storage tank; continuous sampling during the reaction process Analyze the purity of hydrogen chloride, when the hydrogen chloride purity ≥ 95%, it can all be recovered, and when the hy...

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Abstract

The invention belongs to a process for preparing white carbon black and in particular relates to a process for producing precipitated white carbon black by silicon tetrachloride. The process comprises the following steps: adding the silicon tetrachloride into 29 to 33 mass percent hydrochloric acid aqueous solution which contains a dispersant, controlling the temperature to between 28 and 45 DEG C for reaction to generate silica sol and chlorine hydride gas, standing and ageing the silica sol to form colloidal white flocculent sediment, filtering, separating and washing the sediment, and pelletizing and drying the sediment to obtain the precipitated white carbon black. The process has short flow, relatively simple production equipment and process control, and available raw materials, effectively utilizes the silicon tetrachloride, totally reclaims the product chlorine hydride, reduces the processing expense, the amount of waste acid and the environmental pollution, and has low production cost, wide application and large market capacity.

Description

(1) Technical field [0001] The invention belongs to the preparation process of white carbon black, in particular to a process for producing precipitated white carbon black from silicon tetrachloride. (2) Background technology [0002] At present, white carbon black is generally produced by using sodium silicate, silicon tetrachloride, ethyl orthosilicate, etc. as silicon sources. There are two production processes: precipitation method and gas phase method: silicic acid is generally used in the production of white carbon black by precipitation method. Salt (usually sodium silicate) and inorganic acid (usually sulfuric acid) neutralization precipitation reaction method to produce; vapor phase production of white carbon black is the use of silicon chloride (silicon tetrachloride or methyl trichlorosilane) It is produced by high-temperature hydrolysis in a mixed air and hydrogen gas stream, and a large amount of low-purity hydrogen chloride is produced as a by-product during pr...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B33/12
Inventor 王松波王志勇张桂香赵述彬毛晓军吴肖磊焦高成刘娟
Owner 昊华宇航化工有限责任公司
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