<p><i>Pseudomonas reptilivora</i> B-6bs is a promising microbial platform for the industrial production of gluconic, 2-ketogluconic, and 5-ketogluconic acids. This study optimized the production of these metabolites via response surface methodology in a 3-L bioreactor. The experimental design evaluated the effects of the glucose concentration (10–50&#xa0;g/L), aeration rate (0.2–2.0 vvm), and agitation speed (250–600&#xa0;rpm). Metabolite concentrations were determined via specific colorimetric-spectrophotometric methods: the glucose oxidase method for glucose, the Malaprade–Hantzsch reaction for gluconic acid, o-phenylenediamine for 2-ketogluconic acid, and the arsenomolybdate method for 5-ketogluconic acid. The optimization results distinguished between model-predicted optima and experimentally observed outcomes. While the quadratic model suggested a theoretical maximum, the highest experimental efficiency was confirmed in <b>T2</b> (30&#xa0;g/L glucose, 600&#xa0;rpm, and 2.0 vvm), which achieved specific conversion yields (Y<sub>P/S</sub>) of 0.54, 0.84, and 0.97&#xa0;g/g for gluconic, 2-ketogluconic, and 5-ketogluconic acids, respectively, within 24&#xa0;h. Statistical analysis revealed that the glucose concentration was the most significant factor. Further response surface methodology-based optimization suggested an aeration rate of 1.92 vvm at 600&#xa0;rpm to maximize performance. These findings provide a quantitative baseline for the potential development of sustainable bioprocesses using <i>P. reptilivora</i> B-6bs. While scale-up studies are needed, the data suggest that this strain holds promise for biotechnological applications.</p>

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Gluconic and ketogluconic acid production in Pseudomonas reptilivora B-6bs

  • Itan Homero Ruiz-Hernandez,
  • Luis Alberto Madrigal-Perez,
  • Christian Omar Martínez-Cámara,
  • Héctor Eduardo Martínez-Flores,
  • Juan Carlos González-Hernández

摘要

Pseudomonas reptilivora B-6bs is a promising microbial platform for the industrial production of gluconic, 2-ketogluconic, and 5-ketogluconic acids. This study optimized the production of these metabolites via response surface methodology in a 3-L bioreactor. The experimental design evaluated the effects of the glucose concentration (10–50 g/L), aeration rate (0.2–2.0 vvm), and agitation speed (250–600 rpm). Metabolite concentrations were determined via specific colorimetric-spectrophotometric methods: the glucose oxidase method for glucose, the Malaprade–Hantzsch reaction for gluconic acid, o-phenylenediamine for 2-ketogluconic acid, and the arsenomolybdate method for 5-ketogluconic acid. The optimization results distinguished between model-predicted optima and experimentally observed outcomes. While the quadratic model suggested a theoretical maximum, the highest experimental efficiency was confirmed in T2 (30 g/L glucose, 600 rpm, and 2.0 vvm), which achieved specific conversion yields (YP/S) of 0.54, 0.84, and 0.97 g/g for gluconic, 2-ketogluconic, and 5-ketogluconic acids, respectively, within 24 h. Statistical analysis revealed that the glucose concentration was the most significant factor. Further response surface methodology-based optimization suggested an aeration rate of 1.92 vvm at 600 rpm to maximize performance. These findings provide a quantitative baseline for the potential development of sustainable bioprocesses using P. reptilivora B-6bs. While scale-up studies are needed, the data suggest that this strain holds promise for biotechnological applications.