First steps for the scale up of a dual trophies microtubular biofilm reactor - preventing biofilm detachment

<p>The use of phototrophic cyanobacteria in biotechnology is highly interesting as they represent a carbon neutral production platform, relying mainly on carbon dioxide, light and water for growth. However, one key bottleneck for utilizing cyanobacteria as production hosts is that in the currently established cultivation systems like tube or flatpanel reactors only cell densities of 2 to 4 g<sub>CDW</sub>/L are possible, which is at least 20 times too low for most applications. One promising concept to solve this shortcoming is the cultivation of such microbes as dual trophies biofilms in microtubular systems in a segmented flow fashion with air bubbles, as recently reported in [1]. According to the aspects mentioned in Posten et. al [2], it becomes clear that the concept fulfils most requirements for photo-bioreactors. Firstly, the surface area to volume ratio is increasing with decreasing tube diameter. Hence, the path of the light through the reactor is reduced, leading to an optimal light supply. Secondly, using air segments increases the mixing within the reactor leading to a better supply of the cells with a carbon source as well as a better extraction of oxygen. Apart from that, the attached biofilm provides continuous cell regeneration and thus a continuous production system. All these aspects lead to a biomass concentration in this reactor system of up to 60 g<sub>CDW</sub>/L [1].</p> <p>The microtubular system was successfully applied in the challenging conversion of cyclohexane to cyclohexanol [1]. The reaction was conducted in a small lab scale system utilizing capillaries of 20 cm length, with a total volume of 1.4 mL. Here, we are evaluating the impact of larger scale on biofilm performance. Experiments were conducted in 1 m capillaries with 3 mm inner diameter. First, the impact of different flow rates was investigated. Results show, that a total minimal flow rate of 104 µL/min (52 µL air and 52 µL medium /min) leads to a significant biofilm detachment in various positions in the tube after one week of cultivation. A total flow rate of 520 µL/min (260 µL air and 260 µL medium /min) prevents detachment, however, it seems to hinder full surface coverage of the tube. An optimal condition turned out to be a cultivation of the biofilm with a starting flowrate of 520 µL/min for the initial attachment of the cells and a consecutive decrease of the flow to 104 µL/min after one week of cultivation. Thereby biofilm detachment was prevented and full surface coverage was achieved, while scaling the system by 5 fold. Respective data will be presented and discussed.</p> <p>[1] Hoschek, Heuschkel, Mixed-species biofilms for high-cell-density application of <em>Synechocystis</em> sp. PCC 6803 in capillary reactors for continuous cyclohexane oxidation to cyclohexanol, Bioresource Technology, 2019</p> <p>[2] Posten, Design principles of photo-bioreactors for cultivation of microalgae, Engineering in Life Sciences, 2009</p>