Rodríguez Alberto, Hernández-Herreros Natalia, García José L, Auxiliadora Prieto M
Interdisciplinary Platform for Sustainable Plastics towards a Circular Economy-of the Spanish National Research Council (SusPlast-CSIC), Madrid, Spain.
Polymer Biotechnology Group, Department of Plant and Microbial Biotechnology, Biological Research Center, Margarita Salas"-CSIC, 28040, Madrid, Spain.
Biotechnol Biofuels. 2021 Aug 6;14(1):168. doi: 10.1186/s13068-021-02017-6.
Rhodospirillum rubrum is a purple non-sulphur bacterium that produces H by photofermentation of several organic compounds or by water gas-shift reaction during CO fermentation. Successful strategies for both processes have been developed in light-dependent systems. This work explores a dark fermentation bioprocess for H production from water using CO as the electron donor.
The study of the influence of the stirring and the initial CO partial pressure (p) demonstrated that the process was inhibited at p of 1.00 atm. Optimal p value was established in 0.60 atm. CO dose adaptation to bacterial growth in fed-batch fermentations increased the global rate of H production, yielding 27.2 mmol H l h and reduced by 50% the operation time. A kinetic model was proposed to describe the evolution of the molecular species involved in gas and liquid phases in a wide range of p conditions from 0.10 to 1.00 atm.
Dark fermentation in R. rubrum expands the ways to produce biohydrogen from CO. This work optimizes this bioprocess at lab-bioreactor scale studying the influence of the stirring speed, the initial CO partial pressure and the operation in batch and fed-batch regimes. Dynamic CO supply adapted to the biomass growth enhances the productivity reached in darkness by other strategies described in the literature, being similar to that obtained under light continuous syngas fermentations. The kinetic model proposed describes all the conditions tested.
深红红螺菌是一种紫色非硫细菌,它可通过几种有机化合物的光发酵或在CO发酵过程中的水煤气变换反应产生氢气。在光依赖系统中已开发出这两种过程的成功策略。本研究探索了一种以CO作为电子供体从水中生产氢气的暗发酵生物过程。
对搅拌和初始CO分压(p)影响的研究表明,该过程在p为1.00 atm时受到抑制。最佳p值确定为0.60 atm。在分批补料发酵中使CO剂量适应细菌生长提高了氢气生产的总体速率,产率为27.2 mmol H₂ l⁻¹ h⁻¹,并将操作时间缩短了50%。提出了一个动力学模型来描述在0.10至1.00 atm的广泛p条件下气相和液相中所涉及分子物种的演变。
深红红螺菌中的暗发酵扩展了从CO生产生物氢的途径。本研究在实验室生物反应器规模上优化了该生物过程,研究了搅拌速度、初始CO分压以及分批和分批补料操作方式的影响。适应生物质生长的动态CO供应提高了在黑暗条件下通过文献中描述的其他策略所达到的生产率,与在连续合成气光发酵下获得的生产率相似。所提出的动力学模型描述了所有测试条件。