A kind of preparation method of chlorinated polyvinyl chloride for paint, coating and fiber
A chlorinated polyvinyl chloride, paint technology, applied in the chemical characteristics of fibers, coatings, textiles and papermaking, etc., can solve the problems of long time, large nitrogen consumption, long time for normal pressure acid blowing, etc., to achieve investment and steam Reduced consumption, increased production capacity and considerable economic benefits
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
example 1
[0024] Chlorinated polyvinyl chloride for the preparation of paints. at 5m 3 Add chlorinated benzene (chlorinated benzene content > 99.2W / %, polychlorobenzene content ≤ 0.65W / % moisture content ≤ 5 × 10 -5 mass fraction) 3.96 tons, add 0.772 kg of azobisisobutyronitrile, and start stirring until the initiator is completely dissolved in chlorobenzene. Slowly add 396 kg of PVC (polymerization degree 900, oil absorption rate 28), cover the reaction kettle, vacuumize the polymerization kettle to a vacuum degree of 0.08Mpa, and break the vacuum to normal pressure with 0.1Mpa nitrogen. Start to heat up, and control the temperature rise rate to 2°C / min. When the temperature in the reactor is 35°C, the chlorine flow is started, and the chlorine flow rate is 36m 3 / h. When the temperature in the reactor reaches 90°C, increase the chlorine flux to 64m 3 / h. It is advisable that the tail gas basically does not discharge chlorine. When the reaction temperature reached 95°C, the tempe...
example 2
[0029] Chlorinated polyvinyl chloride for the preparation of fibers. at 5m 3 Add chlorinated benzene (chlorinated benzene content > 99.2W / %, polychlorobenzene content ≤ 0.65W / % moisture content ≤ 5 × 10 -5 mass fraction) 3.916 tons, add 0.484 kg of azobisisobutyronitrile, and start stirring until the initiator is completely dissolved in chlorobenzene. Slowly add 484 kg of PVC (polymerization degree 1400, oil absorption rate 32), cover the reaction kettle, vacuumize the polymerization kettle to a vacuum degree of 0.08Mpa, and break the vacuum to normal pressure with 0.1Mpa nitrogen. Start to heat up, and control the temperature rise rate to 2°C / min. When the temperature in the reactor is 35°C, the chlorine flow is started, and the chlorine flow rate is 36m 3 / h. When the temperature in the reactor reaches 90°C, increase the chlorine flux to 64m 3 / h. It is advisable that the tail gas basically does not discharge chlorine. When the reaction temperature reached 95°C, the tem...
PUM
| Property | Measurement | Unit |
|---|---|---|
| adsorption capacity | aaaaa | aaaaa |
| Vicat softening point | aaaaa | aaaaa |
| service temperature | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More