Two-stage series organic silicon slurry and residue drying system and process thereof

By using a two-stage series drying system for organosilicon slurry residue, combined with horizontal and vertical evaporators and a negative pressure distillation tower, the problems of uneven drying, high energy consumption, and low automation in organosilicon slurry residue treatment have been solved, achieving efficient, low-energy continuous drying and resource utilization.

CN122408412APending Publication Date: 2026-07-17JIANGXI BLUESTAR XINGHUO SILICONE CO LTD

Patent Information

Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
JIANGXI BLUESTAR XINGHUO SILICONE CO LTD
Filing Date
2026-04-30
Publication Date
2026-07-17

AI Technical Summary

Technical Problem

Existing organosilicon slurry residue treatment processes suffer from uneven drying, high energy consumption, dispersed emissions of volatiles and harmful gases, low automation levels, and limited applicability, making it difficult to achieve efficient, low-energy continuous drying and resource utilization.

Method used

A two-stage series drying system for organosilicon slurry residue is adopted, including horizontal and vertical evaporators, a negative pressure distillation column, and a gas phase product circulation system. Through heating, stirring, and gas phase separation, continuous drying and deep removal of volatiles from the slurry residue are achieved.

Benefits of technology

It significantly improves drying efficiency, reduces energy consumption, and decreases residual volatiles, enabling continuous, automated, and high-quality treatment of organosilicon slurry residue. It is suitable for the efficient treatment and resource utilization of slurry residue waste in organosilicon production processes.

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Abstract

本发明涉及有机硅副产物处理技术领域,尤其涉及一种两级串联的有机硅浆渣干燥系统及其工艺。包括:卧式蒸发器,设置有加热和搅拌装置,用于对有机硅浆渣进行初步蒸发干燥;立式蒸发器,与所述卧式蒸发器串联连接,所述立式蒸发器的底部设有布气分布器和夹套加热装置,用于对初步干燥后的浆渣进一步蒸发干燥;负压精馏塔,与所述卧式蒸发器和立式蒸发器的气相出口均连通,用于将两个蒸发器产生的气相产物进行分离,并获得塔顶不凝气和其他挥发组分;真空泵,连接于负压精馏塔塔顶,用于对不凝气进行加压;加热器,连接于真空泵出口后,用于将部分不凝气加热至150~250℃;气体循环管路,所述加热后的不凝气经气体循环管路通入所述立式蒸发器的底部,用于实现浆渣废粉流化和进一步干燥。
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