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在搅拌罐式光生物反应器中培养源自海洋红藻细基江蓠的微型植株。

Cultivation of microplantlets derived from the marine red alga Agardhiella subulata in a stirred tank photobioreactor.

作者信息

Huang Yao-Ming, Rorrer Gregory L

机构信息

Department of Chemical Engineering, Oregon State University, Corvallis, Oregon 97331, USA.

出版信息

Biotechnol Prog. 2003 Mar-Apr;19(2):418-27. doi: 10.1021/bp020123i.

Abstract

Macrophytic marine red algae are a diverse source of bioactive natural compounds. "Microplantlet" suspension cultures established from red algae are potential platforms for biosynthesis of these compounds, provided suitable bioreactor configurations for mass culture can be identified. The stirred tank bioreactor offers high rates of gas-liquid mass transfer, which may facilitate the delivery of the CO(2) in the aeration gas to the phototrophic microplantlet suspension culture. Therefore, the effects of impeller speed and CO(2) delivery on the long-term production of microplantlet biomass of the model red alga Agardhiella subulata was studied within a stirred tank photobioreactor equipped with a paddle blade impeller (D(i)/D(T) = 0.5). Nutrient medium replacement was required for sustained biomass production, and the biomass yield coefficient based on nitrate consumption was 1.08 +/- 0.09 g dry biomass per mmol N consumed. Biomass production went through two exponential phases of growth, followed by a CO(2) delivery limited growth phase. The CO(2)-limited growth phase was observed only if the specific growth rate in the second exponential phase of growth was at least 0.03 day(-)(1), the CO(2) delivery rate was less than 0.258 mmol CO(2) L(-)(1) culture h(-)(1), and the plantlet density was at least 10 g fresh mass L(-)(1). Increasing the aeration gas CO(2) partial pressure from 0.00035 to 0.0072 atm decreased the cultivation pH from 8.8 to 7.8, prolonged the second exponential phase of growth by increasing the CO(2) delivery rate, and also increased the photosynthetic oxygen evolution rate. Impeller speeds ranging from 60 to 250 rpm, which generated average shear rates of 2-10 s(-)(1), did not have a significant effect on biomass production rate. However, microplantlets cultivated in a stirred tank bioreactor ultimately assumed compact spherical shape, presumably to minimize exposure to hydrodynamic stress.

摘要

大型海洋红藻是生物活性天然化合物的多样化来源。从红藻建立的“微型植株”悬浮培养物是这些化合物生物合成的潜在平台,前提是能够确定适合大规模培养的生物反应器配置。搅拌罐生物反应器具有较高的气液传质速率,这可能有助于将曝气气体中的二氧化碳输送到光合微型植株悬浮培养物中。因此,在配备桨叶叶轮(D(i)/D(T)=0.5)的搅拌罐光生物反应器中,研究了叶轮转速和二氧化碳输送对模式红藻亚叉节藻微型植株生物量长期生产的影响。持续的生物量生产需要更换营养培养基,基于硝酸盐消耗的生物量产率系数为每消耗1 mmol氮产生1.08±0.09 g干生物量。生物量生产经历了两个指数生长阶段,随后是一个二氧化碳输送受限的生长阶段。只有当第二个指数生长阶段的比生长速率至少为0.03天⁻¹、二氧化碳输送速率小于0.258 mmol CO₂ L⁻¹培养⁻¹小时、植株密度至少为10 g鲜质量L⁻¹时,才会观察到二氧化碳受限的生长阶段。将曝气气体中二氧化碳的分压从0.00035 atm提高到0.0072 atm,可使培养pH从8.8降至7.8,通过提高二氧化碳输送速率延长第二个指数生长阶段,还可提高光合放氧速率。叶轮转速在60至250 rpm之间,产生的平均剪切速率为2至10 s⁻¹,对生物量生产率没有显著影响。然而,在搅拌罐生物反应器中培养的微型植株最终呈现出紧凑的球形,大概是为了尽量减少受到流体动力应力的影响。

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