Open thin-layer cascade reactors for saline microalgae production evaluated in a physically simulated Mediterranean summer climate
Graphical abstract
Introduction
Outdoor mass production of microalgae is poised to impact renewable bio-production of food, chemicals and energy [1]. Algae cultivation is sustainable as it does not compete with agricultural activities and can utilize salt- or waste water, thereby circumventing depletion of valuable fresh water resources [2]. At present, only few high-value industrial products such as pigments are generated by outdoor microalgae processes. For low-value bulk chemicals or biofuels, production cost are currently too high to provide economic viability [3].
The choice of a cultivation system has a major effect on production cost. Open cultivation systems are suitable to generate low-value products [4], [5], [6]. The most widely used open cultivation system is the raceway pond. However, with its depth of 15–30 cm, low cell densities of only 1–1.5 g L−1 are achieved [7], [8], [9]. Hence, energy costs for circulation and harvesting of the algae are high and the cultures are susceptible to contamination [10], [11]. A promising alternative is the thin-layer cultivation concept pioneered in Třeboň, Czech Republic [12], [13], [14]. This bioreactor concept provides for a microalgae suspension to flow down a sloped channel in a layer of < 1 cm thickness. At the end of the channel, the suspension is pumped up again to the starting point. High cell densities of 30–50 g L−1 after 2–3 weeks have been reported in outdoor cultivation of Chlorella and Scenedesmus freshwater strains in the Czech Republic and Greece [15], [16], [17]. Moreover, the microalgae production cost in thin-layer systems were estimated to be only 20% of the cost in raceway ponds [11].
Unfortunately, technical information on thin-layer cascade reactors is scarce [11], [12], [18] and a detailed functional evaluation of all reactor parts is not available, hampering the advancement of thin-layer cultivation. Furthermore, a comparison of different reactor setups is difficult because precise intra-day growth rates have not been determined yet. Moreover, no thin-layer cascades for saltwater have been developed yet, although saline cultivation is desirable because of reduced freshwater use and contamination risk as well as improved CO2 containment in the aqueous phase due to higher pH. Finally, the channels of published thin-layer cascade reactors were made from expensive rigid materials like steel, glass, concrete or fiberglass [19], [20], resulting in a high investment cost compared to other open cultivation systems. Thus, the development of thin-layer cascade reactors addressing these issues appears to be a valuable addition to the growing field of microalgae research.
Testing bioreactors and processes on a larger scale usually requires outdoor experiments. However, achieving a thorough understanding of an outdoor process is complicated by randomly changing environmental conditions. A solution to this is physical and dynamic day and night climate simulation – the realistic indoor reproduction of outdoor environmental conditions [8], [21]. With the recent advent of light-emitting diode (LED) technology in microalgae research [22], faithful sunlight simulation has become possible. Experiments under controlled environmental conditions allow informed decisions on worthwhile improvements. The development process is accelerated since the experiments are independent of outdoor weather conditions. As a result, the investment for a large-scale outdoor microalgae production facility will more likely be profitable if the process has been thoroughly tested and optimized indoors under the environmental conditions of the envisaged outdoor site.
This paper reports on the design, construction, operation, and evaluation of open thin-layer cascade photobioreactors at TUM AlgaeTec Center (Technical University of Munich, Germany), a microalgae research facility enabling physical and dynamic day and night climate simulation on a pilot scale. The LED-supported climate simulation system is presented and the thin-layer cascade reactor design is discussed. The saline microalga Nannochloropsis salina was chosen as a model to evaluate batch process performance in open thin-layer cascade photobioreactors with a surface area of up to 8 m2. In these processes, the climate simulation reproduced the environmental conditions of a Mediterranean summer in Almería, Spain, a suitable location for a large-scale outdoor microalgae cultivation site.
Section snippets
Open thin-layer cascade photobioreactor
The thin-layer cascade reactor design developed and used in this study (Fig. 1) consisted of five modular reactor parts: inlet module, upper channel, flow reversal module, lower channel, and retention tank (parts given in order of the flow of the algae suspension). A detailed technical description of the reactor parts is given in the Supplementary materials.
An off-the-shelf centrifugal pump was used to lift the algae suspension from the retention tank to the inlet module, reducing investment
Growth rates, channel variants, and reactor comparability
Parallel batch processes with the saline microalga Nannochloropsis salina were performed in four thin-layer cascade reactors R1–R4 to evaluate the maximal growth rates in the simulated Mediterranean summer climate and the reactor comparability (Fig. 6). Reactors R1 and R2 were equipped with rigid channels, reactors R3 and R4 were equipped with pond liner channels. The four reactors were situated in the same hall and hence experienced the same environmental conditions (Fig. 6A). The air
Conclusion
Climate simulation – the physical indoor simulation of dynamic outdoor environmental conditions – is an emerging tool in the development of photobioreactors and bioprocesses. In this study, novel open photobioreactors for saline microalgae were designed and evaluated using a globally unique realistic climate simulation technology. In the simulated Mediterranean summer climate of Almería (Spain) – a suitable location for a large-scale outdoor microalgae cultivation site – high growth rates,
Author's contributions
All authors contributed to the conception and design of the study, the interpretation of the data as well as the critical revision and final approval of the manuscript; AA, CP, NB, NM, JG, JS performed the experiments and analyzed the experimental data; AA, DWB wrote the manuscript; TB, DWB obtained the funding.
Acknowledgments
Funding (grant number LaBay74A) provided by the Bavarian State Ministry for Economic Affairs and the Media, Energy and Technology (Munich, Germany), the Bavarian State Ministry of Education, Science and the Arts (Munich, Germany) and Airbus Group (Leiden, The Netherlands) is gratefully acknowledged. Andreas Apel and Christina Pfaffinger were supported by the TUM Graduate School (Technical University of Munich, Germany). The funding sources did not influence the reported research. Stefan Wilbert
References (47)
- et al.
Demonstrated large-scale production of marine microalgae for fuels and feed
Algal Res.
(2015) - et al.
Simulation of outdoor pond cultures using indoor LED-lighted and temperature-controlled raceway ponds and Phenometrics photobioreactors
Algal Res.
(2017) - et al.
Sustainable production of toxin free marine microalgae biomass as fish feed in large scale open system in the Qatari desert
Bioresour. Technol.
(2015) - et al.
An industrial-size flat plate glass reactor for mass production of Nannochloropsis sp. (Eustigmatophyceae)
Aquaculture
(2001) - et al.
Model-based optimization of microalgae areal productivity in flat-plate gas-lift photobioreactors
Algal Res.
(2016) - et al.
Lipid and biomass production by the halotolerant microalga Nannochloropsis salina
Biomass
(1987) - et al.
Rapid salinity measurements for fluid flow characterisation using minimal invasive sensors
Chem. Eng. Sci.
(2017) - et al.
The dark side of algae cultivation: characterizing night biomass loss in three photosynthetic algae, Chlorella sorokiniana, Nannochloropsis salina and Picochlorum sp
Algal Res.
(2015) - et al.
Nannochloropsis production metrics in a scalable outdoor photobioreactor for commercial applications
Bioresour. Technol.
(2012) - et al.
System design for the autotrophic production of microalgae
Enzym. Microb. Technol.
(1985)
Anodic respiration of Pseudomonas putida KT2440 in a stirred-tank bioreactor
Biochem. Eng. J.
Evaluation of carbon dioxide mass transfer in raceway reactors for microalgae culture using flue gases
Bioresour. Technol.
Outdoor production of Scenedesmus sp. in thin-layer and raceway reactors using centrate from anaerobic digestion as the sole nutrient source
Algal Research
Products from microalgae: an overview
Second generation biofuels: high-efficiency microalgae for biodiesel production
Bioenergy Res.
A Look Back at the U.S. Department of Energy's Aquatic Species Program: Biodiesel From Algae
The promise and challenges of microalgal-derived biofuels
Biofuels Bioprod. Biorefin.
A Realistic Technology and Engineering Assessment of Algae Biofuel Production: Energy Biosciences Institute Report
From laboratory to commercial production: a case study of a Spirulina (Arthrospira) facility in Musina, South Africa
J. Appl. Physiol.
High Density Outdoor Microalgal Culture
Novel outdoor thin-layer high density microalgal culture system: productivity and operational parameters
Arch. Hydrobiol. Algol. Stud.
Dual purpose open circulation units for large scale culture of algae in temperate zones. I. Basic design considerations and scheme of a pilot plant
Arch. Hydrobiol. Algol. Stud.
Ivan Šetlík (1928–2009)
J. Appl. Phycol.
Cited by (64)
Cultivation Of Spirulina Platensis for carbon dioxide bio sequestration in hybrid photobioreactor with real-time monitoring system
2024, Journal of Environmental Chemical EngineeringEffects of fluid-flow regimes on Chlorella sorokiniana cultivation in cascade photobioreactors with either flat or wavy bottoms
2022, Journal of BiotechnologyCitation Excerpt :The swirling sections cause a perturbation in the light intensity received by the cells therein. Recently, Chiarini and Quadrio reported that the light/dark cycle in a representative cascade PBR (Apel et al., 2017) was in the range of 0.1–2 s (Chiarini and Quadrio, 2021). The above cycle time was consistent with this range.