Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Process for continuously preparing methyl silicone resin

A technology for the preparation of methyl silicone resin, which is applied in the field of continuous preparation of methyl silicone resin, and can solve the problems of hazards, large investment in equipment, and low production efficiency.

Active Publication Date: 2015-12-02
TANGSHAN SANYOU SILICON IND
View PDF5 Cites 5 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The harm of silicone resin waste water is mentioned in CN101602559B, and the treatment method mentioned in it is comparatively complicated, and it is difficult to realize industrialization
CN103694477A uses alkoxysilane as a raw material to prepare silicone resin, which uses membrane separation and rectification to separate acid medium oil, dilute acid and alcohol, which requires large equipment investment and high energy consumption
Due to the high viscosity of the material and the poor mass and heat transfer effect, the average reaction time of the polycondensation process is 4 to 10 hours. If the polycondensation reaction time is too long, the production efficiency is low and the production energy consumption is large. It is meaningful to develop a reaction device that is more suitable for the polycondensation process. major

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Process for continuously preparing methyl silicone resin

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] A continuous preparation process of methyl silicone resin, carried out as follows:

[0034] Feed according to the following raw material ratio:

[0035] Methyltrichlorosilane: 100kg / h; Dimethyldichlorosilane: 22kg / h; Xylene: 260kg / h.

[0036] Washing dilute acid water: 400kg / h; ethanol: 20kg / h.

[0037] a. Hydrolysis

[0038] Methyltrichlorosilane, dimethyldichlorosilane, and xylene are mixed at a ratio of 5:1:13, and after being initially mixed in a static mixer 11, they enter the tubular hydrolysis reactor 12, where they are washed with dilute acid water and ethanol at a ratio of 20: The ratio of 1 enters the tubular hydrolysis reactor 12, and the washing dilute acid water is dilute hydrochloric acid with a mass concentration of 0.8% (the washing water after the first-level washing in the washing process of the previous kettle material can also be used). The hydrolysis temperature of the material is controlled at 15°C in the hydrolysis system. After the feeding is ...

Embodiment 2

[0052] A continuous preparation process of methyl silicone resin, carried out as follows:

[0053] Feed according to the following raw material ratio:

[0054] Methyltrichlorosilane: 90kg / h; Dimethyldichlorosilane: 32kg / h; Xylene: 250kg / h.

[0055] Washing dilute acid water: 400kg / h; ethanol: 10kg / h.

[0056] a. Hydrolysis

[0057] Methyltrichlorosilane, dimethyldichlorosilane, and xylene are mixed at a ratio of 3:1:8, initially mixed in a static mixer 11, and then entered into a tubular hydrolysis reactor 12, and washed with dilute acid water and ethanol at a ratio of 40: The ratio of 1 enters the tubular hydrolysis reactor 12, and the dilute acid water for washing is dilute hydrochloric acid with a mass concentration of 0.9% (the washing water after the first-level washing in the washing process of the material in the previous kettle can also be used). The hydrolysis temperature of the material is controlled at 20°C in the hydrolysis system. After the feeding is completed...

Embodiment 3

[0071] A continuous preparation process of methyl silicone resin, carried out as follows:

[0072] Feed according to the following raw material ratio:

[0073] Methyltrichlorosilane: 85kg / h; Dimethyldichlorosilane: 35kg / h; Xylene: 240kg / h.

[0074] Washing dilute acid water: 400kg / h; ethanol: 8kg / h.

[0075] a. Hydrolysis

[0076] Methyltrichlorosilane, dimethyldichlorosilane, and xylene are mixed in a ratio of 2.5:1:7, and then enter the tubular hydrolysis reactor 12 after being initially mixed in a static mixer 11, and washed with dilute acid water and ethanol at a ratio of 50: The ratio of 1 enters the tubular hydrolysis reactor 12, and the dilute acid water for washing is dilute hydrochloric acid with a mass concentration of 0.9% (the washing water after the first-level washing in the washing process of the material in the previous kettle can also be used). The hydrolysis temperature of the material is controlled at 25°C in the hydrolysis system. After the feeding is co...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention relates to a process for manufacturing silicone resin, in particular to a process for continuously preparing methyl silicone resin. The process includes steps of hydrolyzing methyl trichlorosilane, dimethyl dichlorosilane and benzene solvents, to be more specific, mixing the methyl trichlorosilane, the dimethyl dichlorosilane and the benzene solvents with one another according to mass ratios to obtain mixtures, feeding the mixtures into a tubular hydrolysis reactor, filling the reactor with alkyl alcohol and washing water with diluted acid according to mass ratios and enabling the methyl trichlorosilane, the dimethyl dichlorosilane, the benzene solvents, the washing water with the diluted acid and the alkyl alcohol to jointly react to one another so as to obtain hydrolysate; washing the hydrolysate by the aid of water by three or more stages until the hydrolysate is neutral; continuously concentrating the hydrolysate in a vacuum state; carrying out condensation polymerization, to be more specific, adding catalysts into the hydrolysate when the effective content of siloxane reaches 50%-60% of kettle volumes, blowing inert gas into the hydrolysate and carrying out condensation polymerization reaction. The process has the advantages that wastewater discharge can be prevented, difficult problems of high discharge of the traditional washing water with acid, high contents of organic matters and difficulty in treating wastewater can be solved, and the product yield can be increased; the inert gas is blown into the hydrolysate in condensation polymerization procedures, accordingly, the low-molecular-weight removal time can be shortened, and yellowing of products can be prevented; system reaction conditions are stable, and the products are excellent in performance.

Description

technical field [0001] The invention relates to a production process of silicone resin, in particular to a continuous preparation process of methyl silicone resin. Background technique [0002] According to different raw materials, the preparation of silicone resin is mainly divided into two routes: alkoxysilane as raw material and chlorosilane as raw material. Due to the low cost of using chlorosilane monomers to produce silicone resins, mainstream products at home and abroad are still produced using chlorosilanes as raw materials. Mixed chlorosilane monomers are hydrolyzed under the protection of benzene-based solvents to prepare methyl silicone resin. In the traditional intermittent hydrolysis process, a large amount of water is required to be washed many times to make the hydrolyzate neutral. The production of 1 ton of silicone resin produces about 10-15 tons of washing wastewater, which not only pollutes the environment, but also reduces the product yield. Benzene-bas...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
IPC IPC(8): C08G77/06C08G77/04
Inventor 孙长江任海涛刘秋艳王春英李献起
Owner TANGSHAN SANYOU SILICON IND
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products