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首页> 外文期刊>Journal of the Chinese Institute of Chemical Engineers >Controlling biofilm growth and lactic acid production by Rhizopus oryzae in a rotating fibrous bed bioreactor: Effects of dissolved oxygen, rotational speed, and urea concentration
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Controlling biofilm growth and lactic acid production by Rhizopus oryzae in a rotating fibrous bed bioreactor: Effects of dissolved oxygen, rotational speed, and urea concentration

机译:在旋转的纤维床生物反应器中控制米根霉生物膜的生长和乳酸的产生:溶解氧,转速和尿素浓度的影响

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摘要

Oxygen was found to be the critical factor affecting lactic acid production by Rhizopus oryzae in a rotating fibrous bed bioreactor (RFBB), which was used to immobilize fungal mycelia and control fungal morphology during fermentation. A lack of oxygen resulted in low lactic acid production because the pathway becomes shunted to ethanol production, and it eventually leads to a loss in fungal activity and cell death. However, simply maintaining a high level of dissolved oxygen (DO) in the RFBB did not significantly improve lactic acid production, whereas increasing oxygen transfer rate led to a slight increase in lactic acid productivity. Ethanol production Occurred even though a high oxygen transfer rate in the fermentation medium was maintained, indicating an anoxic condition occurring in the biofilm due to diffusion limitation. The effective diffusivities of oxygen and glucose in the biofilm were determined experimentally and then used in a. diffusion model to estimate the critical biofilm thickness, which was found to be much smaller than the actual thickness of the biofilm attached on the fibrous matrix, Suggesting the occurrence of oxygen starvation in the overgrown biofilm. Controlling the biofilm thickness to prevent oxygen diffusion limitation could be achieved by shaving off the fungal hyphae at the outer region or limiting cell growth by reducing the nitrogen concentration in the medium. Shaving occurs when the shear stress is higher than the hyphae tensile strength, and the shaving rate is proportional to the specific energy dissipation rate, which in turn is affected by the rotational speed of the fibrous matrix. However, increasing the rotational speed did not improve lactic acid production because the shear stress generated from the fluid motion was not high enough to shave off fungal hyphae. The growth and metabolic pathway of R. oryzae immobilized on the fibrous matrix also can be controlled by manipulating the medium composition, particularly the nitrogen source. It was found that biomass production was limited and lactic acid production increased in the absence of urea in the production phase. However, a lack of nitrogen source could reduce cell activity and product synthesis in long-term cultivation. Therefore, periodical addition of urea during the production phase is recommended to prevent biofilm overgrowth, delay sporulation, and maintain high cell viability and fermentation productivity.
机译:氧气是影响米根霉在旋转纤维床生物反应器(RFBB)中生产乳酸的关键因素,该反应器用于固定真菌菌丝体并控制发酵过程中的真菌形态。缺氧导致乳酸生成量降低,因为该途径与乙醇生成物分路,最终导致真菌活性丧失和细胞死亡。但是,仅在RFBB中保持高水平的溶解氧(DO)并不能显着改善乳酸的产生,而增加的氧气转移速率却会导致乳酸生产率的略微提高。即使维持发酵培养基中的高氧气传输速率,也会发生乙醇生产,这表明由于扩散限制而在生物膜中发生了缺氧状态。通过实验确定生物膜中氧气和葡萄糖的有效扩散率,然后将其用于生物膜中。扩散模型来估计临界生物膜厚度,发现该临界生物膜厚度比附着在纤维基质上的生物膜的实际厚度小得多,这表明在生长过度的生物膜中发生了氧饥饿。控制生物膜的厚度以防止氧扩散受限可以通过在外部区域去除真菌菌丝或通过降低培养基中的氮浓度来限制细胞生长来实现。当剪切应力高于菌丝抗张强度时,就会发生剃刮,并且剃刮速率与比能量耗散率成正比,这又受纤维基质旋转速度的影响。但是,增加旋转速度并不能改善乳酸的产生,因为流体运动产生的剪切应力不足以消除真菌菌丝。固定在纤维基质上的米根霉的生长和代谢途径也可​​以通过操纵培养基组成,特别是氮源来控制。发现在生产阶段中在不存在尿素的情况下,生物质的生产受到限制并且乳酸的生产增加。但是,缺乏氮源可能会降低长期培养中的细胞活性和产物合成。因此,建议在生产阶段定期添加尿素,以防止生物膜过度生长,延缓孢子形成并保持较高的细胞活力和发酵生产力。

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