02050nas a2200217   4500008004100000022001400041245008700055210006900142260000800211300001200219490000700231520134100238653002701579653001301606653002001619653001701639653001501656100002601671700002301697856011201720       2024                        eng d  a2062-249X00aContinuous flow ozonolysis of cardanol for greener synthesis of bio-based monomers0 aContinuous flow ozonolysis of cardanol for greener synthesis of   cJUN  a417-4260 v143 a<p>
	Synthesis of bio-based monomers via continuous flow ozonolysis of cardanol using a simple tubular reactor is demonstrated. The direct ozonolysis of cardanol produces unique monomer 8-(3-hydroxyphenyl) octanal (HPOA) and heptanal along with several other oxidation products. Maximum 47% yield of HPOA with 54.3% conversion of cardanol was obtained at 0 degrees C in 9 s. The complete conversion of cardanol was obtained at the ozone to cardanol molar flow ratios greater than 2 at all temperatures varied in the range of -10 degrees C to 20 degrees C. Owing to large gas-liquid ratios, the mass transfer limitation for transfer of ozone from gas to liquid was negligible; however, the extent of axial dispersion in the liquid phase was significant at lower liquid flow rates. The non-ideal behavior was incorporated in the axial dispersion model to predict the conversion of cardanol. Examination of kinetic rates by both ideal plug-flow model and plug-flow with axial dispersion model revealed that the reaction is fast and is least influenced by the axial-dispersion in the reactor at prevailing operating conditions. The findings of the current study show that continuous flow technique enables a simple and safer synthesis of high-value bio-based monomers via ozonolysis of cardanol compared to traditional batch methods.</p>
10aAxial-dispersion model10aCardanol10acontinuous flow10aHelical coil10aOzonolysis1 aKulkarni, Sphurti, P.1 aKulkarni, Amol, A.  uhttps://library.ncl.res.in/content/continuous-flow-ozonolysis-cardanol-greener-synthesis-bio-based-monomers