Organofunctional silicone copolymers and the saponification products thereof
A technology of siloxane copolymer and hydrolyzate, applied in other chemical processes, coatings, chemical instruments and methods, etc., can solve problems such as poor performance and solid resin turbidity
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Problems solved by technology
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Examples
Embodiment
[0049] Modulator (sulfhydryl-PDMS)
[0050] Mercapto—polydimethylsiloxane, the chain length is about 150 dimethylsiloxane groups and the chain contains about 3 mercaptopropyl groups.
[0051] PDMS mixture
[0052] A mixture of three polydimethylsiloxanes each with a chain length of about 100 dimethylsiloxane units, which contains 5% by weight of non-functionalized polydimethylsiloxane, 20 by weight % Of α-monovinyl polydimethylsiloxane, and 75% by weight of α,ω-divinyl polydimethylsiloxane.
Embodiment 2
[0057] Repeat Comparative Example 1 again, the differences are as follows:
[0058] Initial feed: 737.2 g ethyl acetate, 137.2 g isopropanol, 9.5 g PDMS mixture, 0.5 g PPV and 34.3 g vinyl acetate.
[0059] Initiator feed: 51.4 g ethyl acetate and 2.0 g PPV, the metering rate was 11.5 ml / h, which lasted 310 minutes.
[0060] Monomer feed: 76.2 g of PDMS mixture and 274.3 g of vinyl acetate, the metering rate was 93.4 ml / h, which lasted for 240 minutes.
[0061] The polymerization was subsequently carried out at a temperature of 70°C for 90 minutes. The obtained 1-phase polymer solution is dried according to the above method. As a result, a resin that was transparent at room temperature was prepared.
[0062] Analysis: siloxane copolymer content: 99.0%, gas chromatography analysis: residual vinyl acetate content 0.019%; residual ethyl acetate content 0.8%; residual isopropanol content 0.17%; acid value 2.81 mg KOH / g, viscosity (Hopler, 10% concentration solution in ethyl acetate)=1...
Embodiment 5
[0078] Into a stirring tank with an anchor stirrer, reflux condenser and metering device and a capacity of 120 liters, 34.17 g ethyl acetate, 3.4 kg isopropanol, 189.6 g PDMS mixture, 25.6 g PPV and 1.71 kg vinyl acetate are charged Base ester. Subsequently, the stirring tank was heated to 70°C with a stirring rate of 95 revolutions per minute. After the internal temperature reached 70°C, metered addition of initiator (2.56 g ethyl acetate and 99.7 g PPV) was started at a rate of 512.0 g / h. Ten minutes after the start of the initiator feed, the monomer feed (1.52 kg PDMS mixture and 13.67 kg vinyl acetate) was added at a rate of 3.80 kg / hr. The initiator feed took 310 minutes and the monomer feed was terminated 60 minutes earlier. After the two feeds were terminated, the polymerization was continued at 70°C for 120 minutes. Subsequently, 1000 ml of water was added, and the obtained 1-phase polymer solution was distilled in the stirring tank at a temperature of 95°C, followed by dr...
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Abstract
Description
Claims
Application Information
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