Abstract
Despite the growing interest in photosynthetic microalgae, e.g., as a source of biofuels, the mass cultivation of microalgae still exhibits many drawbacks and successful industrial applications are scarce. Reliable model integrating all relevant phenomena and enabling to assess the system performance, its in silico scale-up and eventually optimization, is still lacking. Here, we present a unified modeling framework for microalgae culture system. We propose a multidisciplinary modeling framework to bridge biology (cell growth) and physics (hydrodynamics and optics) together. This framework consists of (i) the state system (mass balance equations in form of advection-diffusion-reaction PDEs), (ii) the fluid flow equations (Navier-Stokes equations), and (iii) the irradiance distribution. To validate the method, the Couette-Taylor reactor, which hydrodynamically induces the fluctuating light conditions, was chosen. The results of numerical simulation of microalgae growth in this device show good agreement with experimental data.
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Notes
- 1.
Comparing characteristic times of microalgae growth (it is in order of hours) and that of mixing due to dispersion – turbulent diffusion (it is in order of seconds, similarly that of convective transport), one sees that adopting whatever steady state growth model (e.g., Monod, Haldane), only two alternatives exist: (i) to neglect the details concerning mixing phenomena, e.g., by accepting the hypothesis that the entire cell culture dispersed in medium was homogenized at each calculation step (cf. [12], where the time step \(\varDelta t\) for the numerical integration of an underlined model was set to 3600 s), or (ii) to observe the changes due to the hydrodynamic mixing and neglect those of biochemical reaction. Both alternatives completely lose the coupling between transport and reaction phenomena.
- 2.
Couette-Taylor devices are able to generate the so-called Taylor vortex flow (in laminar flow regime) and subsequently oblige microalgae cells to periodically travel between illuminated wall and the dark side of the bioreactor, cf. [24].
- 3.
The same assumption was accepted by J. Pruvost et al. [17] arguing that the smallest eddy size, given by the Kolmogorov scale for their operating conditions, their annular PBR and their microorganism, is ca. ten times greater than the cell size.
- 4.
Photoacclimation, the fourth phenomenon, occurs in the largest scale (days), thus can be represented as a steady state process (via a reaction model parameter) and no differential equation is needed.
- 5.
The PSF model has basically three time constant: one, corresponding to the light and dark reactions, is in order of seconds, other, corresponding to the photoinhibition, is in order of minutes, and finally, the last, which corresponds to microalgae growth, is in order of hours.
- 6.
- 7.
According to Taylor’s explanation [24], the transition between the two regimes is achieved when the viscous forces do not damp the initial infinitesimal disturbances anymore, and this condition is reached when the Taylor number exceeds the given critical value. A further increase of the Taylor number leads to a sequence of two time-dependent flow regime, the wavy vortex flow and the doubly periodic wavy vortex flow.
- 8.
The parameter k represents the attenuation coefficient, unit: \(m^{-1}\), another characteristic parameter describing the attenuation of irradiance by the suspension of microbial cells in the liquid medium is the depth corresponding to the decreasing of the incident irradiance to one half, i.e. \({r_{1/2}} = \frac{\ln 2}{k}\).
- 9.
The Damköhler numbers (Da) are widely used in chemical engineering to relate the chemical reaction timescale (reaction rate) to the transport phenomena rate occurring in a system.
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Acknowledgment
This work was supported by the Ministry of Education, Youth and Sports of the Czech Republic - projects “CENAKVA” (No. CZ.1.05/2.1.00/01.0024) and “CENAKVA II” (No. LO1205 under the NPU I program).
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Appendix
Appendix
Model of Photosynthetic Factory – PSF Model
Here we describe the multi-timescale three-state model of photosynthetic factory (PSF model) proposed by Eilers and Peeters [8] and further developed by Wu and Merchuk [26]. As follows, PSF model is used for the reaction term \(R(c_i)\) derivation, cf. the transport equation (1). PSF model (9) describes the dynamics of three basic phenomena occurring simultaneously in three largely separated time-scales: (i) cell growth (including the shear stress effect), (ii) photoinhibition, and (iii) photosynthetic light and dark reactions. The state vector of the PSF model is three dimensional, \(y=(y_R,y_A,y_B)^{\top }\), where \(y_R\) represents the probability that PSF is in the resting state R, \({y_A}\) the probability that PSF is in the activated state A, and \({y_B}\) the probability that PSF is in the inhibited state B.
The values of model parameters, i.e., \(\alpha ,~\beta , ~\gamma ,~\delta \), and \(\kappa \), cf. 6, are published in Wu and Merchuk (2001) [26]. Concerning the experimental design for parameter estimation and the identifiability study, see [18].
For given input variable, i.e., the irradiance u(t), the ODE system (9) can be solved either by numerical methods or by asymptotic methods. For the special case of the periodic piecewise constant input, the state trajectories were calculated explicitly in [15].
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Papáček, Š., Jablonský, J., Petera, K. (2017). Towards Integration of CFD and Photosynthetic Reaction Kinetics in Modeling of Microalgae Culture Systems. In: Rojas, I., Ortuño, F. (eds) Bioinformatics and Biomedical Engineering. IWBBIO 2017. Lecture Notes in Computer Science(), vol 10209. Springer, Cham. https://doi.org/10.1007/978-3-319-56154-7_60
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