CO2 capture from air by Chlorella vulgaris microalgae in an airlift photobioreactor
Introduction
Human population growth and industrial expansion lead to increased energy consumption and the use of fossil fuels. Fossil fuel combustion releases carbon dioxide (CO2) and water vapour into the atmosphere. The CO2 is a pollutant that causes the greenhouse effect (Basu et al., 2014, Cheah et al., 2015). More than 50 percent of global warming is due to CO2 emissions into the atmosphere. Hence, it is necessary to reduce the uncontrolled emissions of CO2 and to prevent its release into the atmosphere (Wilbanks and Fernandez, 2014). Great efforts have been made by the international community to reduce CO2 emissions in the atmosphere. For instance, the Kyoto Protocol in 1997 and Paris COP 21 in 2015, advocate international restrictions on CO2 release (Nations, 2015).
There are two general approaches to reduce emissions of CO2 into the atmosphere. One way is to reduce consumption of fossil fuels, and the other, moving toward renewable energy, is to capture and utilize CO2. Among the CO2 capture methods, can be cited chemical absorption and the biological fixation process (Chiang et al., 2011, Kaithwas et al., 2012). The biological sequestration process can be performed using plants or microorganisms. Microalgae and cyanobacteria are among the microorganisms that consume CO2 to grow and lead to CO2 fixation. Microalgae and cyanobacteria also have the most conversion efficiency of CO2 into oxygen and biomass products (Chisti, 2007). The CO2 removal by microalgae depends on different parameters such as microalgae species, type of cultivation system, nutrients ratio, light intensity, temperature, pH, CO2 concentration, and gas flow rate (Cheng et al., 2013).
Many studies have been done on CO2 fixation using different algae species. Among them, Chlorella vulgaris, which can tolerate high concentrations of CO2, has high photosynthetic capacity, and can maintain high growth rate and CO2 fixation rate in a wide range of CO2 concentrations from 0.04 to 18% (v/v), can be considered as a good species to fix CO2 (Singh and Singh, 2014, Yang et al., 2015).
Algae cultivation systems play a crucial role in the process of CO2 fixation. There are two types of algae cultivation system for fixing CO2 that include open raceway ponds and closed photobioreactors. Closed photobioreactors compared to open ponds provide better control of operating conditions and increase the efficiency of biofixation (Kasiri et al., 2015, Razzak et al., 2013). Other advantages of the bioreactor in the field of biochemicals are the ease of sterile operations and suitable hydrodynamics for biocatalysts sensitive to the tension and turbulence. Moreover, bioreactors have industrial applications such as in wastewater treatment, and in chemical and biochemical processes (Chisti, 1998).
Different bioreactors could be employed in biochemical processes. Among them, simple bubble column and airlift reactor (ALR) with internal loop and external loop can be cited. ALR has better mixing, more suitable heat, and mass transfer than bubble column due to the existence of the draft tube, and some of its advantages include simple construction without moving parts such as agitator and low consumption of energy (Chen et al., 2016, Chisti, 1998). As CO2 and nutrients are essential for algal growth, ALR hydrodynamic parameters such as gas holdup and liquid circulation velocity play a key role. The gas holdup and liquid circulation velocity are a function of the input gas flow rate (Bitog et al., 2014, Nayak et al., 2014). In addition, the gas flow rate plays a great role in the algae growth, control of pH, creating optimal internal mixing, and preventing the accumulation of oxygen in the system (Kumar et al., 2010). Most of the studies in the CO2 biofixation field have focused on the effect of different levels of CO2, the impact of microalgae species, the effect of temperature, and the effect of light intensity on the rate of CO2 fixation (Basu et al., 2013, Cheng et al., 2013).
The aim of this work was to investigate the effect of high gas superficial velocity on CO2 capture from air using Chlorella vulgaris microalgae and its growth in an airlift photobioreactor with internal loop and internal sparger in constant light intensity and gas CO2 level. This technology reduces CO2 emissions into the atmosphere and helps in reducing global warming. ALR hydrodynamics was also evaluated under different input gas superficial velocities.
Section snippets
Culture medium
Chlorella vulgaris culture used in this study was provided by the Institute of Marine Sciences of Bandar Abbas in the amount of 20 L containing seawater and modified f/2 culture medium of Gillard (Guillard and Ryther, 1962) as nutrient with initial cell concentration about 5 × 106 cell/ml. Each litre of modified f/2 culture medium of Gillard contains 75 g NaNO3, 5 g NaH2PO4·H2O, 30 g Na2SiO3·9H2O, 4.36 g Na2.EDTA, 3.15 g FeCl3·6H2O, 0.18 g MnCl2·4H2O, 0.01 g CoCl2·6H2O, 0.0098 g CuSO4·5H2O, 0.022 g ZnSO4·7H2
The gas holdup
The result showed that with the increase of input gas velocity from 1.627 × 10−3 to 13.281 × 10−3 m/s, the gas holdup increased linearly from 0.0044 to 0.024. The result is in agreement with Blažej et al. (2004) and Popović et al. (2004). At the riser gas superficial velocity lower than 6.955 × 10−3 m/s, the dominant regime was homogeneous bubbly flow. In this region, with increasing the gas superficial velocity, the amount of gas holdup linearly increased up to 0.015. The bubbles in this region were
Conclusion
The study presented that the Chlorella vulgaris has the ability of growth and CO2 capture at high input gas superficial velocities and can resist shear stress. The results showed that with increasing input gas superficial velocity, the gas holdup and liquid superficial velocity in the riser increased. Furthermore, the maximum cell concentration, specific growth rate and CO2 removal efficiency in gas superficial velocity of 7.458 × 10−3 and 13.281 × 10−3 m/s were 23.5 × 106 and 18.3 × 106 cell/ml, 0.2446
Acknowledgements
This work was supported by the Research and Technology Organization and Department of Chemical Engineering of the University of Sistan and Baluchestan, Iran.
Authors would like to express their appreciation to Marine Sciences, Bandar Abbas, Iran for providing the required amount of Chlorella vulgaris microalgae.
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