Method for preparing biomass polyester
A biomass and polyester technology, which is applied in the field of biomass polyester preparation, can solve the problems of poor flexibility of polyester macromolecular segments, high requirements for diol purity, and no description of polymerization process, etc., and achieve stable and excellent performance , maintain stability and reduce energy consumption
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0033] In the reactor, add the terephthalic acid of 166kg and the biomass mixed polyol of 68kg, wherein the biomass mixed polyol comprises the following weight ratio components: ethylene glycol 90wt%, 1,2-propanediol 5wt%, 1,2 -Butanediol 2wt%, pentanediol 2wt%, sorbitol 1wt%; Also add catalyst, thermal stabilizer and antioxidant in following esterification reaction, wherein add catalyst and be titanium dioxide and antimony trioxide, add-on is respectively 250ppm (i.e. 41.5g), adding heat stabilizer is trimethyl phosphate, adding amount is 33g antioxidant is antioxidant 1010, adding amount is 49g; after the above-mentioned components are mixed evenly, at temperature 225 ℃, pressure 0.3Mpa condition The esterification reaction was carried out at a temperature of 3 hours; after the esterification, the product was transported to the polycondensation tank, and the temperature was raised to 260° C. for the polycondensation reaction, and the polycondensation time was 6 hours; the bio...
Embodiment 2
[0035]In the reactor, add the terephthalic acid of 166kg and the biomass mixed polyol of 93kg, wherein the biomass mixed polyol comprises the following weight ratio components: ethylene glycol 99.2wt%, 1,2-propanediol 0.4wt%, 1 , 0.2wt% of 2-butanediol, 0.1wt% of pentanediol, 0.1wt% of sorbitol; In the following esterification reaction, catalyst and heat stabilizer are also added, wherein the catalyst is tetrabutyl titanate, and the addition amount is 120ppm (i.e. 20g), the heat stabilizer is trimethyl phosphate, and the addition amount is 22g; after the above-mentioned components are mixed evenly, the esterification reaction is carried out at 280°C and the pressure of 0.05Mpa, and the reaction time is 2.5h; After melting, the product is transported to the polymerization tank, and at the same time, the temperature is raised to 290° C. for polycondensation reaction, and the polycondensation time is 2 hours; finally, the biomass polyester is obtained.
Embodiment 3
[0037] Add 166kg of terephthalic acid and 80kg of biomass mixed polyols in the reactor, wherein the biomass mixed polyols include the following weight ratio components: ethylene glycol 95wt%, 1,2-propanediol 2wt%, 1,2 -Butanediol 1.5wt%, pentanediol 1wt%, sorbitol 0.5wt%; Catalyst, thermal stabilizer and antioxidant are also added in the following esterification reaction, wherein the catalyst added is antimony trioxide, the content is 500ppm (i.e. 83g); adding heat stabilizer is alkyl phosphoric acid diester, adding amount is 29g, adding antioxidant is antioxidant 168, adding amount is 49g; after mixing evenly, carry out esterification under temperature 240 ℃, pressure 0.2MPa condition Reaction, the reaction time is 3.5h; after esterification, the product is transported to the polymerization tank, and at the same time, the temperature is raised to 280°C for polycondensation reaction, and the polycondensation time is 5h; finally the biomass polyester is obtained.
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com