TY - JOUR
T1 - Photoautotrophic organic acid production
T2 - Glycolic acid production by microalgal cultivation
AU - Kang, Nam Kyu
AU - Kim, Minsik
AU - Baek, Kwangryul
AU - Chang, Yong Keun
AU - Ort, Donald R.
AU - Jin, Yong Su
N1 - Funding Information:
This work was funded by the Realizing Increased Photosynthetic Efficiency (RIPE) that is funded by the Bill & Melinda Gates Foundation, Foundation for Food and Agriculture Research, and the Department for International Development under grant no. OPP1172157 , and the DOE Center for Advanced Bioenergy and Bioproducts Innovation (U.S. Department of Energy, Office of Science, Office of Biological and Environmental Research under award number DE‐SC0018420 ).
Publisher Copyright:
© 2021 Elsevier B.V.
PY - 2022/4/1
Y1 - 2022/4/1
N2 - Although microalgae produce value-added products, such as lipids, pigments, and polysaccharides using light and carbon dioxide, these intracellular products require costly downstream processes such as extraction and purification. Thus, extracellular products are desirable for economic production. While reported before, the secretion of glycolic acid by microalgal photorespiration has not received attention for industrial applications. We developed a two-stage continuous cultivation system to increase glycolic acid production using a glycolate dehydrogenase (GYD1) deficient mutant of Chlamydomonas reinhardtii which produces high concentrations of glycolic acid. Specifically, 3% CO2 was supplied in the first-stage culture for the production of biomass and ambient air (0.03% CO2) was supplied to the second stage for the production of glycolic acid. As a result, overall glycolic acid productivity reached 82.0 mg L-1 d-1 at a dilution rate of 0.34 d-1. However, as the pH of the second stage decreased to 4.7 due to the increased glycolic acid production, we controlled the pH of the second stage at pH 6.0, resulting in 122.6 mg L-1 d-1 of glycolic acid productivity. Flux balance analysis revealed that the experimental glycolic acid production rate was 69% of the theoretical glycolic acid production rate. The deviation might be due to the toxicity of glycolic acid. When a techno-economic analysis was conducted based on the experimental results, the minimum glycolic acid production cost was estimated to be $31 kg−1, indicating a potential for industrial production. These findings suggest that microalgae can be utilized for the cost-effective industrial production of glycolic acid.
AB - Although microalgae produce value-added products, such as lipids, pigments, and polysaccharides using light and carbon dioxide, these intracellular products require costly downstream processes such as extraction and purification. Thus, extracellular products are desirable for economic production. While reported before, the secretion of glycolic acid by microalgal photorespiration has not received attention for industrial applications. We developed a two-stage continuous cultivation system to increase glycolic acid production using a glycolate dehydrogenase (GYD1) deficient mutant of Chlamydomonas reinhardtii which produces high concentrations of glycolic acid. Specifically, 3% CO2 was supplied in the first-stage culture for the production of biomass and ambient air (0.03% CO2) was supplied to the second stage for the production of glycolic acid. As a result, overall glycolic acid productivity reached 82.0 mg L-1 d-1 at a dilution rate of 0.34 d-1. However, as the pH of the second stage decreased to 4.7 due to the increased glycolic acid production, we controlled the pH of the second stage at pH 6.0, resulting in 122.6 mg L-1 d-1 of glycolic acid productivity. Flux balance analysis revealed that the experimental glycolic acid production rate was 69% of the theoretical glycolic acid production rate. The deviation might be due to the toxicity of glycolic acid. When a techno-economic analysis was conducted based on the experimental results, the minimum glycolic acid production cost was estimated to be $31 kg−1, indicating a potential for industrial production. These findings suggest that microalgae can be utilized for the cost-effective industrial production of glycolic acid.
KW - Chlamydomonas reinhardtii
KW - Flux balance analysis
KW - Glycolate dehydrogenase
KW - Glycolic acid
KW - Techno-economic analysis
KW - Two-stage continuous culture
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U2 - 10.1016/j.cej.2021.133636
DO - 10.1016/j.cej.2021.133636
M3 - Article
AN - SCOPUS:85119915356
SN - 1385-8947
VL - 433
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
M1 - 133636
ER -