Growth characteristics of Chlorella sorokiniana in airlift and bubble column photobioreactors
Highlights
► Determination of suitable CO2 concentration for the cell growth of C. sorokiniana. ► Modifying std. TAP [-acetate] medium to control pH drop at higher CO2 concentration. ► Modeling and simulation of the growth profile using logistic equation. ► Comparison of growth profile in airlift and bubble column photobioreactor. ► Comparison of mixing time and KLa in airlift and bubble column photobioreactor.
Introduction
Global warming has reached an alarming level due to increase in CO2 concentration in the atmosphere. Recent studies conducted at Mauna Loa Observatory (Hawaii, US) in December, 2011 found that the concentration of CO2 in air was nearly 391 ppmv. Thus, it is imperative to identify and improve the process of CO2 sequestration. In view of this, microalgae have been identified as a potential candidate for sequestering CO2. Besides mitigating CO2, they are known to have several other uses. They can be used for the production of biofuels (e.g. biodiesel, bioethanol, biohydrogen) and other important products like industrial biofilters, food products and secondary metabolites (Loubiere et al., 2009, Kumar et al., 2011).
Microalgae, Chlorella sorokinina, is playing an important role as food and feed because of the multiuse of its biomass previously known to be a rich source of carbohydrate, vitamins, and proteins. The high protein content makes it a suitable raw material for the production of single cell protein (Mahasneh, 1997) while the high vitamin contents makes it a suitable feed for aquaculture systems (Gapasin et al., 1998). Besides, under sulfur deprived condition (Chader et al., 2009) C. sorokiniana is also known to produce clean energy, biohydrogen. Additionally, it has been used for the production of commercially important antioxidants like lutein, α/β carotene, α/β tocopherol, zeaxanthin (Matsukawa et al., 2000).
Several factors are known to affect the CO2 sequestration process; like choice of photobioreactor, culture/strain, temperature, pH, light intensity, culture density, concentration of CO2, SOx and NOx, CO2 mass transfer, O2 accumulation etc. (Kumar et al., 2011). Among these, most notably, a suitable photobioreactor is essential for improved CO2 sequestration and better utilization of light. Ease of operation, scalability, lower land requirement, higher biomass productivity and cost effectiveness are some of the significant features of an ideal photobioreactor (Kumar et al., 2011). Airlift and bubble column were considered as ideal photobioreactors for the present study because they are known to possess all the above-mentioned properties. In the past, both airlift and bubble column photobioreactors have been studied extensively for the cultivation of shear sensitive microorganisms (Barbosa et al., 2003; Chisti, 1989, Suh and Lee, 2001). Similarly, Ranjbar et al. (2008) and Harker et al. (1996) performed studies on airlift photobioreactor for astaxanthin and carotenoids production respectively. However, till date, these photobioreactors have not been completely exploited for the cultivation of photosynthetic microorganisms. A comparative analysis of both the photobioreactors based on the growth profile of the organism, mixing time and volumetric mass transfer coefficient may provide a thorough and comprehensive knowledge of both of the reactors. However, only few studies are available on the interaction of CO2 mass transfer, light availability, hydrodynamic stress in the airlift photobioreactor (Chisti and Young, 1993; Contreras et al., 1998, Sánchez Miron et al., 2004, Hulatt and Thomas, 2011).
It is well known that alga grows efficiently only at optimal CO2 concentrations while, any further increase or decrease of CO2 concentration limits its growth (Chiu et al., 2008). Similarly, pH is another factor limiting the growth of the microalgae. Mostly the microalgae maintain neutral or slightly alkaline cytosolic pH, as many enzymes are highly pH dependent and become inactive in acidic pH (Gimmler, 2001). Moreover, choice of nitrogen source in the medium is critical as it serves as a nitrogen source as well as, controls the pH of the medium. TAP medium containing NH4Cl has been extensively used by the researchers for the growth of the biomass that can be used for the hydrogen production (Skjanes et al., 2008). However, use of NaNO3 as nitrogen source is considered as better than the NH4Cl especially in presence of high CO2 concentration in the reactor. Chen et al. (2011) reported that inhibition of cell growth at higher CO2 concentration in the presence of NH4Cl may be due inability of cells to regulate passive diffusion of the NH3, which is in equilibrium with , across the plasma membrane. Moreover, consumption of NaNO3 by algae may increase the pH of the medium as also, it may balance the pH drop due to high dissolved CO2 and carbonic acids (Hulatt and Thomas, 2011).
Thus, the present study aimed to determine the growth characteristics of C. sorokiniana in airlift and bubble column photobioreactors based on different aspects like, mixing time, KLa, and growth profile. Besides, the study investigated the effects of factors like pH and CO2 stress on algal growth profile. Further, an attempt was made to modify the existing TAP [-acetate] medium by substituting NH4Cl by NaNO3 to improvise algal cultivation at higher CO2 concentrations.
Section snippets
Microalgae and culture medium
The culture of C. sorokiniana was obtained from Dr. Kari Skjanes (Norwegian Institute for Agricultural and Environmental Research, Bioforsk, Oslo, Norway). The microalgae were cultured in TAP medium having composition as described below (Skjanes et al., 2008). TAP media contained 2.42 g L−1 Tris base, 25 ml L−1 TAP salt stock solution (15.0 g L−1 NH4Cl, 4.0 g L−1 MgSO4 7H2O, 2.0 g L−1 CaCl2 2H2O, 0.375 ml L−1 PO4 stock solution (28.8 g per 100 ml K2HPO4, 14.4 g per 100 ml KH2PO4), 1 ml L−1 Hutner trace metals
Growth profile in TAP [-acetate] medium
Different concentrations of CO2 in air using the TAP [-acetate] medium were studied in airlift photobioreactor. As shown in Fig. 2a at 5% air–CO2 concentration maximum biomass of 1.8 g L−1 was obtained which corresponded to 3.24 g L−1 of CO2 sequestered. Net specific growth rate in TAP [-acetate] medium were 0.84, 1.13, 1.45, 1.26, 1.1 day−1 at air, 2%, 5%, 8%, 10% air–CO2 gas mixture (v/v) respectively while the maximum biomass concentration corresponded to 1.1, 1.4, 1.8, 0.8, 0.3 g L−1.
Effect of medium modifications
Effect of pH
Conclusions
Five percent CO2 in air (v/v) was found suitable for the cultivation of C. sorokiniana yielding PE and maximum biomass of 7.1%, 4.4 g L−1 respectively. mTAP [-acetate] medium was found to be effective in preventing the rapid decline of pH at higher CO2 concentrations. Defined cyclic mixing pattern was observed in airlift reactor compared to its random pattern in the bubble column. This may be one of the reasons for the better growth performance of airlift reactor. Besides, in airlift, KLa of
Acknowledgement
The authors wish to thank the financial support by the Royal Norwegian Embassy, New Delhi, India (Project BioCO2).
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