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Continuous enzymatic polymerization of phenol in a liquid-solid circulating fluidized bed

机译:液固循环流化床中苯酚的连续酶促聚合

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摘要

A liquid-solid circulating fluidized bed (LSCFB) system consisting of 3.8 cm I.D.and 4 m high riser and 12 cm I.D.and 3.5 m high down-comer was investigated in this study for the continuous polymerization of phenol.Approximately 8.5 kg immobilized particles containing soybean seed hull peroxidase enzymes were applied in the LSCFB system.The continuous enzymatic polymerization was carried out in the riser section by introducing phenol and hydrogen peroxide at the entrance of the riser.Under optimized hydrodynamic conditions and by keeping the molar concentration ratio of phenol to H_2O_2 of 1:2,54% conversion of phenol was achieved.The down-comer of the LSCFB was utilized for the regeneration of the coated immobilized enzyme particles.The effect of the superficial liquid velocity and an initial substrate concentration was studied.Our experimental results show that an enzymatic reaction and the regeneration of the biocatalysts can be carried out simultaneously and independently in the LSCFB system.Furthermore,this work opens the possibilities for many bioprocesses where the deactivation of the biocatalysts is a major problem and the regeneration of the biocatalysts is required.
机译:本研究研究了由3.8 cm IDand 4 m高立管和12 cm IDand 3.5 m高降管组成的液固循环流化床(LSCFB)系统,用于苯酚的连续聚合。约8.5 kg固定化颗粒包含在LSCFB系统中应用大豆种子壳过氧化物酶,在立管段通过在立管进口处引入苯酚和过氧化氢进行连续的酶促聚合反应。在最佳水动力条件下,并保持苯酚与苯酚的H_2O_2的转化率为1:2,54%。利用LSCFB的降液管再生固定的包被的酶颗粒,研究了表面液速和初始底物浓度的影响。结果表明,酶促反应和生物催化剂的再生可在LS中同时独立进行CFB系统。此外,这项工作为许多生物过程打开了可能性,在这些过程中,生物催化剂的失活是一个主要问题,需要生物催化剂的再生。

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