A continuous preparation process of high-purity and low-viscosity simethicone oil
A simethicone oil and preparation technology, which is applied in the field of continuous preparation process of high-purity and low-viscosity simethicone oil, can solve the problems of easy damage of ion exchange resin, volume expansion, impact on de-lowering effect and product quality, etc. Achieve the effects of reducing the difficulty of equipment processing, increasing the capping rate, ensuring catalytic activity and product quality
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0032] Dimethicone mixed ring (DMC) and end-capping agent (MD 2M) According to the mass ratio of 100:4.92, transport it to the pretreatment tank, first use liquid nitrogen to freeze and remove water, control the freezing temperature to -10°C, freeze and remove water for 2 hours, freeze and remove water and then transport it to the mixed drying tank , after heating up to 50°C, the vacuum degree is controlled at -0.085~-0.095Mpa, while stirring, dry nitrogen (nitrogen after vaporization of liquid nitrogen) is introduced to carry out deep dehydration for 2 hours, and the mixture after deep dehydration is sequentially dewatered by a vortex pump It is sent to stainless steel filter and ultrafiltration membrane filter for filtration to remove ions and solid impurities, and then sent to the preheater to preheat to 80°C, and then sent to the fluidized bed equipped with LDX-604 macroporous cation exchange resin Medium reaction, the reaction temperature is controlled at 60°C, and the re...
Embodiment 2
[0034] The dimethylsiloxane mixed ring body (DMC) and the end-capping agent (MDM) are transported to the pretreatment tank at a mass ratio of 100:2.16, and the water is first frozen with liquid nitrogen, and the freezing temperature is controlled at -5°C , the freezing and dehydration time is 3 hours, after freezing and dehydrating, it is transported to the mixed drying kettle. After the temperature is raised to 40°C, the vacuum degree is controlled at -0.090~-0.095Mpa, and dry nitrogen is introduced while stirring (the nitrogen gas after the liquid nitrogen is vaporized ) after deep dewatering for 3 hours, the mixture after deep dewatering is sent to stainless steel filter and ultrafiltration membrane filter to filter through vortex pump to remove ions and solid impurities, and then sent to preheater to preheat to 40 ℃, and then transported to the fluidized bed equipped with D72H macroporous cation exchange resin for reaction, the reaction temperature is controlled at 30 ℃, an...
Embodiment 3
[0036] Dimethicone mixed ring (DMC) and end-capping agent (MD 3 M) According to the mass ratio of 100:1.48, transport to the pretreatment tank, first use liquid nitrogen to freeze and remove water, control the freezing temperature to -15°C, freeze and remove water for 1h, freeze and remove water and then transport it to the mixed drying tank , the vacuum degree is controlled at -0.085~-0.095Mpa. After the temperature is raised to 70°C, dry nitrogen gas (nitrogen after vaporization of liquid nitrogen) is introduced while stirring to carry out deep water removal for 1 hour, and the mixture after deep water removal is removed by a vortex pump. Sequentially transported to stainless steel filter, ultrafiltration membrane filter to remove ions and solid impurities, and then transported to the preheater to preheat to 100 ° C, and then transported to the fluidized bed equipped with D72H macroporous cation exchange resin Reaction, the reaction temperature is controlled at 90°C, and the...
PUM
| Property | Measurement | Unit |
|---|---|---|
| water content | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 