Manufacturing method and use for chlorinated polyvinyl chloride resin
US-2024010762-A1 · Jan 11, 2024 · US
US10035865B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10035865-B2 |
| Application number | US-201515326810-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 21, 2015 |
| Priority date | Jul 22, 2014 |
| Publication date | Jul 31, 2018 |
| Grant date | Jul 31, 2018 |
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The present disclosure relates to a process for the preparation of CPVC which includes reacting PVC with chlorine at a pre-determined temperature in the presence of at least one irradiation source having wavelength ranging from 254 and 530 nm while maintaining the radiant flux from 1.5 to 2 W/kg of PVC, irradiance at 0.13 W/cm 2 and the number of photons emitted per second from 3×10 18 to 5×10 18 , under agitation, for a time period ranging from 3 to 4 hours to obtain CPVC. The CPVC prepared from the afore-stated process has a whiteness index ranging from 89 to 96, a yellowness index ranging from 1.23 to 1.73 and stability ranging from 648 to 684 seconds. The rate of the chlorination reaction after employing the afore-stated process parameters ranges from 1.6 to 4.36 mole/hour/kg.
Opening claim text (preview).
The invention claimed is: 1. A process for the preparation of chlorinated polyvinyl chloride (CPVC) comprising reacting polyvinyl chloride (PVC) with chlorine at a pre-determined temperature in the presence of at least one irradiation source having wavelength ranging from 254 and 530 nm while maintaining the radiant flux from 1.5 to 2 W/kg of PVC, irradiance at 0.13 W/cm 2 and the number of photons emitted per second from 3×10 18 to 5×10 18 , under agitation, for a time period ranging from 3 to 4 hours to obtain CPVC, said obtained CPVC being characterized by a whiteness index ranging from 89 to 96, a yellowness index ranging from 1.23 to 1.73 and thermal stability at 210° C. ranging from 648 to 684 seconds. 2. The process as claimed in claim 1 , wherein said PVC is in at least one form selected from the group consisting of PVC in completely dried form characterized by 0.2 to 1% loss on heating at 70° C. for 2 hours and PVC in slurry form having concentration ranging from 10 to 30% w/v. 3. The process as claimed in claim 1 , wherein the porosity of said PVC ranges from 0.26 to 0.28 ml/g. 4. The process as claimed in claim 1 , wherein said irradiation source is a narrow spectral band width source having a wavelength in the range of 254 to 530 nm. 5. The process as claimed in claim 1 , wherein said pre-determined temperature ranges from 50 to 90° C.
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