Here, we present a protocol to construct lab-scale bubble column photobioreactors and use them to culture microalgae. It also provides a method for the determination of the culture growth rate and neutral lipid content.
There is significant interest in the study of microalgae for engineering applications such as the production of biofuels, high value products, and for the treatment of wastes. As most new research efforts begin at laboratory scale, there is a need for cost-effective methods for culturing microalgae in a reproducible manner. Here, we communicate an effective approach to culture microalgae in laboratory-scale photobioreactors, and to measure the growth and neutral lipid content of that algae. Instructions are also included on how to set up the photobioreactor system. Although the example organisms are species of Chlorella and Auxenochlorella, this system can be adapted to cultivate a wide range of microalgae, including co-cultures of algae with non-algae species. Stock cultures are first grown in bottles to produce inoculum for the photobioreactor system. Algae inoculum is concentrated and transferred to photobioreactors for cultivation in batch mode. Samples are collected daily for the optical density readings. At the end of the batch culture, cells are harvested by centrifuge, washed, and freeze dried to obtain a final dry weight concentration. The final dry weight concentration is used to create a correlation between the optical density and the dry weight concentration. A modified Folch method is subsequently used to extract total lipids from the freeze-dried biomass and the extract is assayed for its neutral lipid content using a microplate assay. This assay has been published previously but protocol steps were included here to highlight critical steps in the procedure where errors frequently occur. The bioreactor system described here fills a niche between simple flask cultivation and fully-controlled commercial bioreactors. Even with only 3-4 biological replicates per treatment, our approach to culturing algae leads to tight standard deviations in the growth and lipid assays.
The application of microalgae in engineering and biotechnology has attracted great interest in recent years. Microalgae are being studied for use in wastewater treatment1,2,3,4, biofuel production5,6,7,8, and the production of nutraceuticals and other high value products9,10. Algae are also being genetically modified at greater rates in an effort to improve their fitness for specific engineering applications11,12. Consequently, there is great interest in experimentation with industrially relevant organisms in controlled settings. The purpose of this method is to communicate an effective approach to culture microalgae in a controlled laboratory environment, and to measure the growth and neutral lipid content of that algae. Improving growth rates and neutral lipid content of microalgae have been identified as two key bottlenecks toward commercialization of algal biofuels13.
A wide range of approaches have been used to culture algae for experimental purposes. In general, these approaches can be divided between large-scale outdoor cultivation and small-scale indoor cultivation. Outdoor cultivation in photobioreactors and open ponds is appropriate for experimentation aimed at scaling up processes that have already been proven at laboratory scale (e.g., to test scale-up of a new high-lipid strain of algae)14. However, indoor small-scale cultivation is appropriate when developing new or improved algae strains or performing experiments aimed at understanding biological mechanisms. In these latter cases, a high-degree of experimental control is required to tease out subtle changes in biological behavior. To that end, axenic cultures are often required in order to minimize the complex biotic factors associated with other organisms (e.g. bacteria, other algae) that inevitably grow in large-scale outdoor systems. Even when studying interactions among algae and other organisms, we have found that use of highly-controlled experimental conditions is helpful when examining molecular exchange among organisms15,16,17.
Within the category of small-scale indoor algae cultivation, a range of approaches have been used. Perhaps the most common approach is to grow algae in Erlenmeyer flasks on a shaker table beneath a light bank18,19. Exchange of oxygen and CO2 takes place by passive diffusion through a foam plug in the top of the flask. Some researchers have improved this set-up through active aeration of the flasks20. Another approach is to cultivate algae in bottles, mixed by stir bar and active aeration. Despite their simplicity, we have found that the use of flasks and bottles often leads to inconsistent results among biological replicates. Presumably this is due to position effects – different positions receive different amounts of light, which also affect internal reactor temperatures. Daily rotation of reactors to new positions can help but does not alleviate the problem because certain stages of algae growth (e.g., early exponential) are more sensitive to positional effects than others (e.g., log phase).
On the opposite side of the spectrum of technological sophistication are fully-controlled commercial photobioreactors. These systems continuously monitor and adjust conditions in the reactor to optimize algae growth. They have programmable lighting, real-time temperature control, and pH control. Unfortunately, they are expensive and typically cost several thousand dollars per reactor. Most scientific and engineering journals require biological replication of results, necessitating the purchase of multiple bioreactors. We present here a bubble column reactor system that bridges the divide between the simple (flask) and sophisticated (fully-controlled bioreactor) approaches for lab-scale algae cultivation. Bubble columns use rising gas bubbles to facilitate gas exchange and mix the reactor. This approach provides some degree of control over the lighting and temperature but does so in a way that is cost-effective. Moreover, we have found this system to yield highly consistent results among biological replicates, reducing the required number of biological replicates needed in order to obtain statistically significant results when compared to the flask or bottle approach. We have also used this system to successfully cultivate mixtures of algae and bacteria21. In addition to algae cultivation, we outline a procedure for measuring the neutral lipid content in the cultured algae. The latter method has been published elsewhere22, but we include the procedure here to provide step-by-step instructions for how to employ it successfully.
1. Setup of Bubble Column Photobioreactors
Figure 1. Schematic and photos for constructing bioreactors. (A) Schematic for construction of the bioreactor lids (B) photo of the assembled bioreactor lid, and (C) photo of the assembled lid used for the humidifier. Note that the humidifier fittings should be coated in water-proof silicone to ensure an airtight seal with the lid. Please click here to view a larger version of this figure.
Figure 2. Schematic and photos for assembling bubble column system. (A) Schematic of the aeration system (B) photo of the humidifier, mixing trap, and rotameter bank, and (C) photo of the manifolds used to connect the rotameter banks together. Please click here to view a larger version of this figure.
Figure 3. System schematic for the bottle bioreactors (left) and the bubble column photobioreactors (right). This figure has been modified from Higgins et al.17. Please click here to view a larger version of this figure.
2. Preparation of Microalgae Inoculum
3. Cultivation of Microalgae in Bubble Column Photobioreactors
4. Harvest and Freeze Drying of Microalgal Biomass
5. Lipid Extraction using a Modified Folch method24
6. Neutral Lipid Assay using a Microplate Method (adapted from Higgins et al. 201422)
This procedure yields a time course of algal optical density data at OD 550 nm (Figure 4A). The optical density and dry weight concentration data can be correlated (Figure 4B). This is accomplished by first calculating the final dry weight algae concentration after the freeze-drying step. Next, the optical density of the culture serial dilution (performed on the last day of sampling) and the actual dry weight concentrations can be correlated. For low cell concentrations, a linear correlation can be used whereas for higher cell concentrations, a second order polynomial correlation may be used. It is recommended to create a separate correlation for each culture condition. Finally, the correlation can be applied to the time course optical density data to obtain a dry weight growth curve (Figure 4C). In this example experiment, Auxenochlorella protothecoides (UTEX 234125) was cultured under four conditions: axenic control cultures grown on fresh N8-NH4 medium21, in co-culture with the bacteria Azospirillum brasilense, in medium supplemented with 50 mg/L of indole-3-acetic acid, and on spent medium from A. brasilense. A. brasilense is known to produce indole-3-acetic acid, a plant growth promoting hormone, that also promotes growth in some microalgae. However, at 50 mg/L, the IAA treatment completely inhibited A. protothecoides growth. Consequently, optical density data was available, but the quantity of algae was insufficient to obtain an accurate dry weight concentration. In this case, the correlation for the control culture may be applied or optical density data may be reported directly. Because OD data was collected at both 550 nm and 680 nm absorbance, either dataset may be used for the correlation between OD and dry weight. Typically, OD 550 is used because it almost completely excludes the absorbance of chlorophyll26, thus suppressing bias from changes in chlorophyll content. In contrast, OD 680 includes the absorbance of chlorophyll and high ratios of OD 680/550 indicate high chlorophyll content in the algae. Figure 4D shows a set of twelve algae cultures growing in the bubble column photobioreactors. Even with only three biological replicates per treatment, tight standard deviations were achieved, allowing for high sensitivity to differences among treatments.
Figure 4. Algae growth results in bubble column photobioreactors. (A) The optical density (550 nm) growth curve of Auxenochlorella protothecoides (UTEX 2341) shows cultures entering late logarithmic growth at 120 hours. Control cultures were grown on fresh N8-NH4 medium, treatment 1 is co-cultures of A. protothecoides and Azospirillum brasilense grown on fresh N8-NH4 medium, treatment 2 is axenic A. protothecoides grown on N8-NH4 medium supplemented with 50 mg/L indole-3-acetic acid (IAA), and treatment 3 is axenic A. protothecoides grown on spent medium from A. brasilense. The spent medium was prepared by culturing A. brasilense for 96 hours on N8-NH4 medium supplemented with 2 g/L malic acid. Cells were removed, and the medium was re-supplemented with ammonium to restore its initial level, pH was adjusted, and the medium was sterile filtered (0.2 μm). Note that the 50 mg/L IAA treatment completely inhibited algae growth. (B) Correlation curves between OD 550 nm and final dry weight concentration using a second order polynomial fit. No correlation is shown for treatment 2 because no algae could be harvested at the end of the culture period. (C) Application of the polynomial correlation to the optical density data yields a growth curve with dry weight concentration on the y-axis. The control culture correlation was applied to the OD data for treatment 2. Error bars are standard deviations based on 3 biological replicates. (D) Photo of the bubble column photobioreactors shortly after culture inoculation. Please click here to view a larger version of this figure.
Neutral lipid data is shown for two example experiments in Figure 5. This assay has been shown to correlate well with neutral lipid content, particularly triacyglycerol (TAG) content. This can be seen by comparing the neutral lipid assay (Figure 5A) to a corresponding thin layer chromatography plate (Figure 5B). The same trend can be seen in the second experiment (Figure 5C and 5D). In all of these experiments, canola oil was used as a standard and resulted in a linear correlation (R2 of 0.98 for the first experiment and 0.99 for the second) between fluorescence and canola oil mass in the well. Note that if all samples have low lipid content, then the highest point or two on the standard may be dropped. This correlation can be used to calculate the quantity of neutral lipid (µg) in each of the algae sample wells. The oil mass can then be converted to a concentration in the lipid extract applied to the microplate well. This value is multiplied by the dilution factor used (e.g., 3x) to obtain the neutral lipid content of the original Folch extracts. This concentration is then multiplied by the volume of the extract (should be close to 4 mL) and then divided by the total mass of algae biomass used for lipid extraction (should be close to 20 mg). The result is the neutral lipid content of the microalgae.
Figure 5. Neutral lipid data obtained from cultures of Chlorella sorokiniana (UTEX 2714). (A) Neutral lipid content (% dry weight) for algae in experiment 1 in which algae were grown for 120 hours. The control culture was axenic and cultured on fresh N8 medium23, treatment 1 was a co-culture of C. sorokiniana and A. brasilense on fresh N8 medium, treatment 2 was fresh N8 medium supplemented with 50 mg/L IAA, and treatment 3 was spent medium from A. brasilense. The spent medium was prepared by culturing A. brasilense for 96 hours in N8 medium supplemented with 2 g/L malic acid, removing cells, supplementing lost nitrate, adjusting pH, and sterile filtering the medium (0.2 μm). Unlike A. protothecoides, 50 mg/L of IAA did not inhibit C. sorokiniana growth. (B) TLC plate image for experiment 1 showing relative TAG abundance. (C) Neutral lipid content (% dry weight) for algae in experiment 2 which had the same treatments as experiment 1 but the cells were harvested after 72 hours of growth. (D) TLC plate image for experiment 2 showing relative TAG abundance. Error bars are standard deviations based on 3 biological replicates. Please click here to view a larger version of this figure.
Also, it is good practice to calculate the coefficient of variation (standard deviation divided by the mean) of the raw fluorescence readings across all technical replicates in the neutral lipid assay. Assuming technical replicates were carried out in the microplate in quadruplicate as noted in the procedure, the coefficient of variation typically should not exceed 10%. High coefficients of variation are usually the result of poor mixing (particularly during the addition of isopropyl alcohol) and potentially inaccurate use of the multichannel pipette.
The most important consideration when culturing algae is an understanding of the specific needs of the organism or group of organisms. The algae cultivation system described here can be used to culture a wide range of algae but the specific abiotic factors (temperature, media, pH, light intensity, CO2 level, aeration rate) need to be adjusted to the needs of the organism. Note the parameters described here were used for the cultivation of Chlorella and Auxenochlorella. These organisms are of industrial interest because they are tolerant to high nutrient, light, and temperature levels27. However, light levels can be reduced through removal of fluorescent bulbs and the day/night cycle can be adjusted to represent seasonality. Likewise, the water heaters can be turned up or down to control the water bath temperature on the system. While the system described here does not employ such a feature, it is possible to chill the fish tank water baths below room temperature through a low-cost cooling system. Place a bucket of water in a small refrigerator and use a variable speed pump to pump water from the cold-water bucket to the fish tank and back. The faster the pumping rate, the colder the fish tank reservoir will become.
Although the algae cultivation system generally provides consistent results, there are a few important caveats that should be considered. The first is water siphoning that occurs in the event that the aeration system experiences a sudden loss of pressure (e.g., a blown fitting or an air compressor failure). Pressure that is in the humidifiers will push humidifier water backward through the tubing, including through the rotameter. Installing an upstream trap or backflow preventer can help. Note that siphoning will not impact the bioreactors themselves because they operate at atmospheric pressure. Routine inspection of the piping and fittings can help alleviate system failures. Another important consideration is to routinely inspect and replace air filters and check valves on the bioreactors. Be sure to follow the manufacturer's recommendation for the number of autoclave cycles allowable. This is particularly important if maintenance of axenic cultures is critical to the experiment. Finally, it is recommended to purchase or construct an autoclavable rack for safe transport of the bioreactors between the water baths, autoclave, and biosafety cabinet. A stainless-steel wire rack can serve this purpose.
The bioreactor system described here has several limitations. A key limitation is the need to handle the reactors in a biosafety cabinet using sterile technique. The reactors lack an anti-siphoning sampling port, requiring the user to move the reactor to a biosafety cabinet to sample without contaminating the culture. The reactors also require manual pH reading and adjustment which introduces potential for human error.
The bioreactor system described here fills a niche between simple flask cultivation and fully-controlled bioreactors. The bioreactor system was developed in response to a need for more consistent results than were achievable using bottles. The data shows that this system generates consistent growth results when operated appropriately. Note that aerated bottles were employed in the procedure for cultivation of algae stock, but this was done only to produce inoculum for the experiment. This is acceptable because stock bottles were pooled for inoculation and hence variability among reactors is not an issue.
As many algae researchers are interested in monitoring both growth and neutral lipid content, we have included our approach to measuring both of these parameters here. Use of optical density to measure growth is standard practice and is unparalleled in its simplicity. However, correlations between dry weight and optical density change over time and depend on culture conditions. It is recommended to produce a correlation equation for each experimental treatment within every experimental batch. This is possible in the proposed procedure because freeze dried algae will be obtained after every culture experiment. A critical assumption of the optical density approach is that the correlation between optical density and dry weight holds constant over the course of batch growth. As long as deviations from this assumption are small, the result will be reasonably accurate. The relative accuracy can be assessed by comparing the calculated algae dry weight concentration at time zero. Assuming cultures were well mixed, and pipetting was accurate, all of the cultures should have the same initial inoculation density. The optical density approach can also be challenged when background absorbance of the medium is high (i.e., when working with certain wastewaters). Subtraction of the medium absorbance (prior to inoculation) from each OD reading can help with this issue.
Extraction of lipids from the dry algae follows the well-established Folch approach21,24; however, there are important considerations. Different algae species have different cell walls with varying degrees of toughness. The zirconia/silica beads used here are sharp and are designed to pierce strong, polysaccharide cell walls. A softer bead type (e.g., glass) or fewer bead disruption cycles may be used on algae with weaker cell walls. However, a rule of thumb is that the resulting cell pellet after extraction should be free of pigment, indicating that all chlorophyll was extracted. One of the most common sources of failure during the lipid extraction step occurs due to improper freeze drying. If the sample melts in the freeze dryer before it is fully dry, the result will be a very hard, dark, waxy pellet. This is the result of cells that lysed under the vacuum conditions of the freeze dryer. The pellet may be weighed to obtain a dry weight, but it cannot be used for lipid extraction as the waxy particles do not break down in the Folch solvent. To ensure that freeze drying always yields soft, powdery samples, it is essential to freeze all samples to -80 °C and promptly transfer them to the freeze dryer. Moreover, using parafilm (with a hole poked in it) rather than loosened tube lids will ensure that moisture can be continuously removed from the sample before it thaws.
The neutral lipid assay described in this procedure has been published previously and includes a discussion of alternative lipid assays22. However, some important improvements have been made to that procedure since publication. Most notably, the Nile red solution concentration was increased from 0.5 µg/mL to 1 µg/mL. The effect of this change was higher signal intensity, improved repeatability, and an elimination of signal decline over time during the incubation period. The results show that the assay compares well to results from qualitative thin layer chromatography. This assay was developed and validated using various species of Chlorella and Auxenochlorella so its applicability to species of significantly different composition has not been determined. All green pigment should be completely removed from the assay during the bleach incubation, leading to samples that are clear or very pale yellow. Also note that lipid extracts that are degraded (as indicated by a change from green to brown color) typically fail to deliver accurate results in this assay. It is thus imperative to store lipid samples at no higher than -20 °C in the dark.
The methods presented here for culturing algae, measuring growth, and quantifying neutral lipids are useful for a variety of engineering applications of algae, but are particularly suitable for research on biofuel production. These methods are also being used to study algal growth inhibition on wastewaters28 as well as impacts of organism interaction on the growth and composition of microalgae.
The authors have nothing to disclose.
Support for this research was provided by USDA National Institute of Food and Agriculture Hatch Project ALA0HIGGINS and the Auburn University Offices of the Provost, the Vice President for Research, and the Samuel Ginn College of Engineering. Support was also provided by NSF grant CBET-1438211.
Supplies for airlift photobioreactor setup | |||
1 L Pyrex bottles | Corning | 16157-191 | For bottle reactors, humidifiers |
1/2" hose clamp | Home Depot | UC953A | or equivalent |
1/4" female luer to barb | Nordson biomedical | Nordson FTLL360-6005 | 1/4" ID, PP |
1/4" ID, 3/8" OD autoclaveable PVC tubing | Thermo-Nalgene | 63013-244 | 50' |
1/4" in O-rings | Grainger | 1REC5 | #010 Medium Hard Silicone O-Ring, 0.239" I.D., 0.379"O.D. |
1/8" Female luer to barb | Nordson biomedical | FTLL230-6005 | |
1/8" ID, 1/4" OD autoclaveable PVC tubing | Thermo-Nalgene | 63013-608 | 250' |
1/8" male spinning luer to barb | Nordson biomedical | MLRL013-6005 | |
1/8" multiport barb | Nordson biomedical | 4PLL230-6005 | 1/8" multiport barb |
1/8" NPT to barb | Nordson biomedical | 18230-6005 | 1/8" 200 series barb |
1/8" panel mount luer | Nordson biomedical | Nordson MLRLB230-6005 | 1/8", PP |
10 gallon fish tank | Walmart | 802262 | Can hold up to 8 bioreactors depending on layout |
100-1000 ccm flow meter | Dwyer | RMA-13-SSV | For bottle reactors |
2 ft fluorescent light bank | Agrobrite | FLT24 T5 | |
200-2500 ccm flow meter | Dwyer | RMA-14-SSV | For air regulation upstream of humidifier |
250 mL Pyrex bottles | Corning | 16157-136 | For gas mixing after humidifier |
50-500 ccm flow meter | Dwyer | RMA-12-SSV | For hybridization tube reactors |
5-50 ccm flow meter | Dwyer | RMA-151-SSV | For CO2 flow rate control |
Air filters 0.2 µm | Whatman/ Fisher | 09-745-1A | Polyvent, 28 mm, 0.2 µm, PTFE, 50 pack |
Check valves | VWR | 89094-714 | |
Corning lids for pyrex bottles | VWR | 89000-233 | 10 GL45 lids |
Female luer endcap | Nordson biomedical | Nordson FTLLP-6005 | Female stable PP |
Hybridization tubes | Corning | 32645-030 | 35×300 mm, pack of 2 |
Light timer | Walmart | 556393626 | |
Locknuts | Nordson biomedical | Nordson LNS-3 | 1/4", red nylon |
Low profile magnetic stirrer | VWR | 10153-690 | Low profile magnetic stirrer |
Male luer endcap | Nordson biomedical | Nordson LP4-6005 | Male plug PP |
Spinning luer lock ring | Nordson biomedical | Nordson FSLLR-6005 | |
Stir bars – long | VWR | 58949-040 | 38.1 mm, for bottle reactors |
Stir bars – medium | VWR | 58949-034 | 25 mm, for hyridization tubes |
Supplies and reagents for culturing algae | |||
0.2 µm filters | VWR | 28145-491 | 13 mm, PTFE, for filtering spent media from daily culture sampling |
1 mL syringes | Air-tite | 89215-216 | For filtering spent media from daily culture sampling |
1.5 mL tubes | VWR | 87003-294 | Sterile (or equivalent) |
10 mL Serological pipettes | Greiner Bio-One | 82050-482 | Sterile (or equivalent) |
100 mm plates | VWR | 25384-342 | 100×15 mm stackable petri dishes, sterile |
15 mL tubes | Greiner Bio-One | 82050-276 | Sterile (or equivalent), polypropylene |
2 mL Serological pipette tips | Greiner Bio-One | 82051-584 | Sterile (or equivalent) |
2 mL tubes | VWR | 87003-298 | Sterile (or equivalent) |
50 mL tubes | Greiner Bio-One | 82050-348 | Sterile (or equivalent), polypropylene |
96 well microplate | Greiner Bio-One | 89089-578 | Polystyrene with lid, flat bottom |
Inocculating loops | VWR | 80094-478 | Sterile (or equivalent) |
Liquid carbon dioxide tank and regulator | Airgas | CD-50 | |
Supplies and reagents for lipid extraction and neutral lipid assay | |||
2 mL bead tubes | VWR | 10158-556 | Polypropylene tube w/ lid |
96 well microplates | Greiner Bio-One | 82050-774 | Polypropylene, flat bottom |
Bleach | Walmart | 550646751 | Only use regular bleach, not cleaning bleach |
Chloroform | BDH | BDH1109-4LG | |
Dimethyl sulfoxide | BDH | BDH1115-1LP | |
Isopropyl alcohol | BDH | BDH1133-1LP | |
Methanol | BDH | BDH20864.400 | |
Nile red | VWR | TCN0659-5G | |
Pasteur pipette tips | VWR | 14673-010 | |
Sodium chloride | BDH | BDH9286-500G | |
Vegetable oil | Walmart | 9276383 | Any vegetable oil should work as long as it is fresh |
Zirconia/ silica beads (0.5 mm diameter) | Biospec products | 11079105z | |
Equipment | |||
Analytical balance | Mettler-Toledo | XS205DU | Capable of at least 4 decimal accuracy |
Bead homogenizer | Omni | 19-040E | |
Benchtop micro centrifuge | Thermo | Heraeus Fresco 21 with 24×2 | Including rotor capable of handling 1.5 and 2 mL tubes |
Dry block heater | VWR | 75838-282 | Including dry block for a microplate |
Freeze dryer | Labconco | 7670520 | 2.5L freeze drying system |
Large benchtop centrifuge | Thermo | Heraeus Megafuge 16R Tissue | Including rotors capable of handling 400 mL bottles, 50 mL tubes, and 15 mL tubes |
Microplate reader | Molecular Devices | SpectraMax M2 | Capable of reading absorbance and fluorescence |
Vortex mixer | VWR | 10153-838 |