2020
DOI: 10.1016/j.jcou.2019.12.023
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Efficient CO2 capture from the air for high microalgal biomass production by a bicarbonate Pool

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Cited by 56 publications
(24 citation statements)
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“…These results indicated that 0.42 g L −1 NaHCO 3 with 2% CO 2 was the optimal carbon source for biomass production and CO 2 fixation, which was consistent with the previous reports that the highest biomass productivity (0.14 g L −1 d −1 ) of C. vulgaris was achieved under 5 mmol L −1 NaHCO 3 with 5% CO 2 as the carbon source ( Lohman et al, 2015 ). More encouragingly, compared to the latest reports so far, R CO2 (544.21 mg L −1 d −1 ) obtained in the shake flasks was superior to that of 360.12 mg L −1 d −1 for Chlorella fusca ( Zhu et al, 2020 ), 350.0 mg L −1 d −1 for Scenedesmus sp. ( Rodas-Zuluaga et al, 2021 ), 470.0 mg L −1 d −1 for Chlorella sp.…”
Section: Resultssupporting
confidence: 54%
See 1 more Smart Citation
“…These results indicated that 0.42 g L −1 NaHCO 3 with 2% CO 2 was the optimal carbon source for biomass production and CO 2 fixation, which was consistent with the previous reports that the highest biomass productivity (0.14 g L −1 d −1 ) of C. vulgaris was achieved under 5 mmol L −1 NaHCO 3 with 5% CO 2 as the carbon source ( Lohman et al, 2015 ). More encouragingly, compared to the latest reports so far, R CO2 (544.21 mg L −1 d −1 ) obtained in the shake flasks was superior to that of 360.12 mg L −1 d −1 for Chlorella fusca ( Zhu et al, 2020 ), 350.0 mg L −1 d −1 for Scenedesmus sp. ( Rodas-Zuluaga et al, 2021 ), 470.0 mg L −1 d −1 for Chlorella sp.…”
Section: Resultssupporting
confidence: 54%
“…In addition to DIC, the most stable pH in the medium was also observed under the optimal carbon source (0.42 g L −1 NaHCO 3 and 2% CO 2 ) with the minimum pH fluctuation at 1.15, compared to 1.47 in the control and around 1.94 in the other two cultures ( Figure 1C ). It was reported that bubbled CO 2 captured by the hybrid carbon source (NaHCO 3 and CO 2 ) and stored as HCO 3 − could drop the pH value in the medium and weaken the effect of pH rise resulting in nitrate and HCO 3 − consumption via algal cell growth ( Wang et al, 2018 ; Zhu et al, 2020 ). When HCO 3 − is utilized, OH − can be released and then recycled to capture subsequent CO 2 to form bicarbonate again ( Gardner et al, 2012 ).…”
Section: Resultsmentioning
confidence: 99%
“…In this situation, carbon supply and mixing cannot be decoupled. Compared with CO 2 gas, a high concentration of bicarbonate can supply sufficient carbon for microalgae growth , and continuous mixing may not be obligate. For instance, the mixing in floating PBRs that use bicarbonate as the sole carbon source can use intermittent wave energy as the driving force. , Therefore, a periodical mixing mode may support good growth of microalgae, which may greatly reduce the mixing cost.…”
Section: Introductionmentioning
confidence: 99%
“…89 Microalgae can survive in saline, alkaline and waste water, but high pH conditions increase the gas-liquid mass transfer rate of CO 2 and biomass productivity, potentially increasing the feasibility of DAC (e.g., in nature, soda lakes encourage such microalgae processes). 333,334 Suspension-based techniques, e.g., open ponds or photobioreactors, can have large land, water, energy and maintenance requirements, and significant gas-liquid mass transfer limitations. Open pond systems, however, are easily scalable and offer lower costs and energy requirements than alternative arrangements, with such an approach being piloted by Global Algae (Table 1).…”
Section: Assessment Of Alternative Processes For Direct Air Capturementioning
confidence: 99%