Production method for chlorinated vinyl chloride resin
A technology of chlorinated vinyl chloride and a manufacturing method, which is applied to the manufacturing field of chlorinated vinyl chloride resins, and can solve the problems of poor heat resistance stability, no control, and inability to obtain transparent molded products.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Publication Date
- 2016-11-09
- Estimated Expiration
- Not applicable · inactive patent
Smart Images
Figure 1
Abstract
Description
technical field
[0001] The present invention relates to a method for producing a chlorinated vinyl chloride-based resin having high initial coloring properties, high heat resistance stability, excellent thermal stability, and a transparent molded product. Background technique
[0002] Chlorinated vinyl chloride resins are produced by post-chlorination of vinyl chloride resins, and have the advantages of vinyl chloride resins, such as excellent weather resistance, flame retardancy, and chemical resistance, and are compatible with vinyl chloride resins. It is 20 to 40°C higher than the heat deflection temperature, so it can be suitably used in applications requiring heat resistance of 100°C, such as heat-resistant pipes, heat-resistant joints, heat-resistant valves, and heat-resistant plates.
[0003] However, since chlorinated vinyl chloride resins have a high heat distortion temperature, they must be heated and melted at high temperatures in order to be molded into heat-resi...
Examples
Embodiment 1
[0075] Put 200 kg of deionized water and 56 kg of vinyl chloride resin with an average degree of polymerization of 600 into a glass-lined reaction container with an internal volume of 300 liters, stir to disperse the vinyl chloride resin in water to form a water suspension state, and then heat the inside of the reaction container Instead, the aqueous suspension was warmed to 70°C.
[0076] Then, after reducing the pressure in the reaction vessel to remove oxygen (oxygen content 100 ppm), chlorine (oxygen content 50 ppm) was introduced so that the chlorine partial pressure was 0.4 MPa to start thermal chlorination (chlorination start temperature 70° C.).
[0077] Then, the temperature was raised to 90° C. over 1.1 hours so as to reach a temperature not higher than the glass transition temperature of the partially chlorinated vinyl chloride resin.
[0078] In addition, the glass transition temperature of a partially chlorinated vinyl chloride resin is calculated|required by DSC ...
Embodiment 2
[0086] Put 200 kg of deionized water and 56 kg of vinyl chloride resin with an average degree of polymerization of 600 into a glass-lined reaction container with an internal volume of 300 liters, stir to disperse the vinyl chloride resin in water to form a water suspension state, and then heat the inside of the reaction container Instead, the aqueous suspension was warmed to 70°C.
[0087] Then, after reducing the pressure in the reaction vessel to remove oxygen (oxygen content 100 ppm), chlorine (oxygen content 50 ppm) was introduced so that the chlorine partial pressure was 0.4 MPa to start thermal chlorination (chlorination start temperature 70° C.).
[0088] Then, the temperature was raised to 95° C. over 1.4 hours so as to reach a temperature not higher than the glass transition temperature of the partially chlorinated vinyl chloride resin.
[0089]Thereafter, after the chlorine content of the partially chlorinated vinyl chloride resin was 60.7% by weight, the temperature...
Embodiment 3
[0095] Put 200 kg of deionized water and 56 kg of vinyl chloride resin with an average degree of polymerization of 600 into a glass-lined reaction container with an internal volume of 300 liters, stir to disperse the vinyl chloride resin in water to form a water suspension state, and then heat the inside of the reaction container Instead, the aqueous suspension was warmed to 70°C.
[0096] Then, after reducing the pressure in the reaction vessel to remove oxygen (oxygen content 100 ppm), chlorine (oxygen content 50 ppm) was introduced so that the chlorine partial pressure was 0.4 MPa to start thermal chlorination (chlorination start temperature 70° C.).
[0097] Then, the temperature was raised to 100° C. over 2.0 hours so as to reach a temperature not higher than the glass transition temperature of the partially chlorinated vinyl chloride resin.
[0098] In addition, the glass transition temperature of a partially chlorinated vinyl chloride resin is calculated|required by DSC...