Bio-Based Epoxy Polymers, Blends, and Composites. Группа авторов

Bio-Based Epoxy Polymers, Blends, and Composites - Группа авторов


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(Table 1.5), it was observed that the incorporation of PTCP into DGEBA epoxy resin accelerates the thermal degradation process and improves the char yield.

      The same higher char yield is valuable toward improving the flame‐retardant properties of epoxy resins. The LOI value of EP/PTCP‐30% increases from 23.0% (neat epoxy material) to 30.5%. Moreover, compared with neat epoxy resin, the impact strength of EP/PTCP‐30% increases by 29%.

      Cardanol is an interesting nonedible by‐product of CNSL industry. Because of the presence of phenolic hydroxyl group, olefinic linkages in the alkyl chain, and aromatic ring, it is a promising nonharmful renewable substituent to BPA. The presence of long aliphatic chain of cardanol in bio‐based epoxy resins results in lower Tg values of obtained materials than those with DGEBA. At the same time, these materials are characterized by very interesting thermal stabilities. Moreover, the mechanical properties of cardanol‐based epoxies are lower than DGEBA epoxies. However, numerous, described in the literature, studies tested coating applications of epoxies obtained with the cardanol derivatives.

Schematic illustration of the synthesis of PTCP.
Sample Thermal properties Mechanical properties
T10% (°C) Tmax1 (°C) Tmax2 (°C) Char residue (%) LOI (%) Impact strength (kJ/m2) Tensile modulus (GPa) Tensile strength (MPa) Elongation at break (%)
PTCP 286 322 500 2.8
EP 361 367 554 1.4 23.0 14.9 ± 1.1 1.56 ± 0.10 40.6 ± 2.5 2.2 ± 0.8
EP/PTCP‐10% 336 344 554 4.2 26.5 16.8 ± 1.0 1.35 ± 0.00 46.3 ± 3.4 5.5 ± 01
EP/PTCP‐20% 328 344 575 5.7 28.0 18.1 ± 1.4 1.46 ± 0.03 60.8 ± 4.4 7.7 ± 1.8
EP/PTCP‐30% 311 335 577 8.3 30.5 19.1 ± 0.5 1.09 ± 0.09 46.7 ± 1.1 8.2 ± 0.4
Chemical structures of isosorbide. Schematic illustration of the pathway for the production of bio-based isosorbide.

      1.3.4 Isosorbide

      The synthesis of isosorbide can start from polysaccharides (mainly starch or cellulose biomass) or directly from all of the intermediate compounds because they are currently commercially available on a large scale. Lignocellulosic biomass is considered as one of the best resource due to its abundancy, versatility, and price [121]. The synthetic process of isosorbide production from polysaccharides consists of the following stages: acid‐catalyzed hydrolysis of the glycosidic bonds in the polymeric carbohydrates, hydrogenation of obtained glucose to sorbitol and further dehydration to sorbitan, and finally dehydration of sorbitan to isosorbide. Moreover, the different side reactions (such as degradation or polymerization) can occur in this complex process. Therefore, different new synthesis strategies (including the one‐step synthesis from glucose and cellulose) and catalysts are still elaborated and proposed [122].

Chemical reaction of the possible reaction pathways for the synthesis of the diepoxide derivative of isosorbide.
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