2012
DOI: 10.1016/j.bej.2012.07.013
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A critical evaluation of CO2 supplementation to algal systems by direct injection

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Cited by 73 publications
(32 citation statements)
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“…Although bacterial contamination and CO2 escape is not a problem in a photobioreactor, the operation and sterilization of numerous photobioreactors are laborious, time-consuming, and costly (Kumar, 2015). Several researchers have also reported that CO2 gas-liquid mass transfer rates are still a factor inhibiting the growth of autotrophic microalgae in a photobioreactor (Fan, 2008;Langley, 2012;Pirouzi, 2014). Fan et al (Fan, 2008) constructed a membrane sparged helical tubular photobioreactor in order to overcome the CO2 mass transfer limitations during C. vulgaris cultivation.…”
Section: Introductionmentioning
confidence: 99%
“…Although bacterial contamination and CO2 escape is not a problem in a photobioreactor, the operation and sterilization of numerous photobioreactors are laborious, time-consuming, and costly (Kumar, 2015). Several researchers have also reported that CO2 gas-liquid mass transfer rates are still a factor inhibiting the growth of autotrophic microalgae in a photobioreactor (Fan, 2008;Langley, 2012;Pirouzi, 2014). Fan et al (Fan, 2008) constructed a membrane sparged helical tubular photobioreactor in order to overcome the CO2 mass transfer limitations during C. vulgaris cultivation.…”
Section: Introductionmentioning
confidence: 99%
“…In contrast, consider that Langley et al . reported that the carbon capture rate was only 2.1% when feeding carbon dioxide at mole fractions of 1.45% to a Chlorella vulgaris culture in an internal loop air lift reactor. Therefore, the prospect that a TVAR could be used to simultaneously capture waste stream carbon dioxide and produce useful products motivates further investigation and development of Taylor vortex algal photobioreactors.…”
Section: Resultsmentioning
confidence: 99%
“…The observation that high carbon dioxide capture rates (70%) can be sustained over long periods of time in a continuous flow TVAR using a high CO 2 mole fraction (10%) is also significant since this concentration is typical of those found in fossil fuel power plant flue gases [15]. In contrast, consider that Langley et al [16] reported that the carbon capture rate was only 2.1% when feeding carbon dioxide at mole fractions of 1.45% to a Chlorella vulgaris culture in an internal loop air lift reactor. Therefore, the prospect that a TVAR could be used to simultaneously capture waste stream carbon dioxide and produce useful products motivates further investigation and development of Taylor vortex algal photobioreactors.…”
Section: Resultsmentioning
confidence: 99%
“…In particular, the observation that high algal growth rates can be obtained in a TVAR at high CO 2 mole fractions (10%) is significant, as these concentrations approach those typically found in fossil fuel flue gas streams (12-15%), and the possibility of simultaneously capturing carbon and producing useful products from these waste streams by feeding them to algal PBRs is highly attractive (Packer, 2009). Based upon studies of the effects of CO 2 feed gas mole fraction on algal productivity in airlift reactors, however, some have questioned the efficacy of direct injection of flue gases into algal reactors (Langley et al, 2012), but the results presented here are more encouraging. Lastly, we note that in addition to potential commercial applications Taylor vortex algal reactors hold near-term promise as laboratory-scale reactors capable of significantly reducing the time required to develop high concentration cultures that otherwise grow slowly in shake flask, airlift, or bubble column reactors.…”
Section: Discussionmentioning
confidence: 99%