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首页> 外文期刊>Journal of microbiology and biotechnology >Catalytic biofilms on structured packing for the production of glycolic acid
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Catalytic biofilms on structured packing for the production of glycolic acid

机译:规整填料上的催化生物膜用于生产乙醇酸

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While structured packing modules are known to be efficient for surface wetting and gas-liquid exchange in abiotic surface catalysis, this model study explores structured packing as a growth surface for catalytic biofilms. Microbial biofilms have been proposed as selfimmobilized and self-regenerating catalysts for the production of chemicals. A concern is that the complex and dynamic nature of biofilms may cause fluctuations in their catalytic performance over time or may affect process reproducibility. An aerated continuous trickle-bed biofilm reactor system was designed with a 3 L structured packing, liquid recycling and pH control. Pseudomonas diminuta established a biofilm on the stainless steel structured packing with a specific surface area of 500 m~2 m~(-3) and catalyzed the oxidation of ethylene glycol to glycolic acid for over two months of continuous operation. A steady-state productivity of up to 1.6 gl~(-1)h~(-1) was achieved at a dilution rate of 0.33 h~(-1). Process reproducibility between three independent runs was excellent, despite process interruptions and activity variations in cultures grown from biofilm effluent cells. The results demonstrate the robustness of a catalytic biofilm on structured packing, despite its dynamic nature. Implementation is recommended for whole-cell processes that require efficient gas-liquid exchange, catalyst retention for continuous operation, or improved catalyst stability.
机译:虽然已知结构填充模块对于非生物表面催化中的表面润湿和气液交换非常有效,但该模型研究探索了结构填充作为催化生物膜的生长表面。已经提出微生物生物膜作为用于生产化学品的自固定和自再生的催化剂。令人担忧的是,生物膜的复杂和动态特性可能会导致其催化性能随时间波动或可能影响过程的可重复性。设计了充气连续滴流床生物膜反应器系统,该系统具有3升规整填料,液体循环和pH值控制。假单胞菌在比表面积为500 m〜2 m〜(-3)的不锈钢结构填料上建立了生物膜,并连续两个月以上催化乙二醇氧化为乙醇酸。在0.33 h〜(-1)的稀释率下,稳态生产率达到1.6 gl〜(-1)h〜(-1)。尽管从生物膜流出细胞生长的培养物中存在过程中断和活性变化,但三个独立运行之间的过程重现性非常好。结果证明了催化生物膜在结构填料上的坚固性,尽管其具有动态性质。建议对需要高效气液交换,催化剂保持连续运行或提高催化剂稳定性的全电池工艺实施。

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