Production method for improving heat stability of polyvinyl chloride resin
A polyvinyl chloride resin and thermal stability technology, which is applied in the production field of improving the thermal stability of polyvinyl chloride resin, can solve the problems of low whiteness of products, poor initial coloring ability, etc., prolong the cleaning cycle and solve the initial discoloration problem , The effect of eliminating the thermal degradation trigger site
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0036] The production process after the improvement of the production process of polyvinyl chloride resin is as follows: figure 2 As shown, the details are as follows:
[0037] (1) After coating the kettle, start the main feeding procedure, first add buffer, then add pure water, vinyl chloride monomer, dispersant 1, dispersant 2, and initiator in sequence;
[0038] (2) After the reaction is completed, add the compound fatty acid zinc and terminator to terminate the reaction; use the discharge pump to pump the slurry in the kettle into the discharge tank, and then strip and further dry it through the stripper;
[0039] Taking the production process of SG5 type PVC resin as an example, the above process is further introduced in detail as follows:
[0040] (1) at 70m 3 In the reaction kettle, after coating the kettle, start the main feeding procedure, and add 60kg of buffer, 31t of pure water, 25.5t of vinyl chloride monomer, 285kg of dispersant 1, 150kg of dispersant 2, and 9...
Embodiment 2
[0050] Identical to the preparation method in Example 1, the present embodiment only appropriately adjusted the consumption of adding fatty acid zinc, and the addition of each material is:
[0051] at 70m 3 Add 60kg of buffer, 31t of pure water, 25.5t of vinyl chloride monomer, 285kg of dispersant 1, 150kg of dispersant 2, and 90kg of initiator into the reactor in sequence;
[0052] The polymerization reaction temperature was 56.5°C, and 40kg of terminator and 7kg of fatty acid zinc were added after the reaction;
[0053] The concrete type of each material is with embodiment 1.
Embodiment 3
[0055] Identical to the preparation method in Example 1, the present embodiment only appropriately adjusted the consumption of adding fatty acid zinc, and the addition of each material is:
[0056] at 70m 3 Add 60kg of buffer, 31t of pure water, 25.5t of vinyl chloride monomer, 285kg of dispersant 1, 150kg of dispersant 2, and 90kg of initiator into the reactor in sequence;
[0057] The polymerization reaction temperature is 56.5°C, and 40kg terminator and 8kg fatty acid zinc are added after the reaction is completed;
[0058] The concrete type of each material is with embodiment 1.
PUM
| Property | Measurement | Unit |
|---|---|---|
| alcoholysis degree | aaaaa | aaaaa |
| alcoholysis degree | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 