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Gellan gum has been widely used in many industries due to its excellent physical properties. In this study, the effects of different fermentation conditions on molecular weight and production of gellan gum were analyzed, and the optimized fermentation conditions for a high molecular weight gellan gum (H-GG: 6.42 × 10 5  Da) were obtained, which increased the molecular weight and yield of gellan gum by 201.4 % and 44.9 % respectively. Fourier transform infrared spectroscopy (FT-IR) and x-ray diffraction (XRD) analysis indicated that H-GG has similar characteristic absorption and semi-crystalline structures with the initial gellan gum (I-GG), and it was composed of glucose, rhamnose, and glucuronic acid showing no obvious changes in the molecular structure. Scanning electron microscope (SEM) observation revealed that the filaments of H-GG were slender, longer, and looser with larger pores. Importantly, gel properties analysis showed that the gel strength, viscoelasticity, and water-holding capacity of H-GG were better than those of I-GG, and the rheological results revealed that the H-GG is a pseudoplastic fluid with higher apparent viscosity and stable viscoelasticity at 20-70 °C. Therefore, the molecular weight and yield of gellan gum are significantly affected by fermentation conditions, and the obtained H-GG demonstrates improved gel and rheological properties., Competing Interests: Declaration of competing interest We declare that we have no financial and personal relationships with other people or organizations that can inappropriately influence our work, there is no professional or other personal interest of any nature or kind in any product, service and/or company that could be construed as influencing the position presented in, or the review of, the manuscript entitled, “Effect of fermentation conditions on molecular weight, production, and physicochemical properties of gellan gum”., (Copyright © 2024. Published by Elsevier B.V.)

3-Hydroxypropionic acid (3-HP) is one of the 12 valuable platform chemicals with versatile applications in the chemical, food, and cosmetic industries. However, the biosynthesis of 3-HP faces challenges due to the lack of robust chassis and the high costs associated with the fermentation process. To address these challenges, we made efforts to augment the robustness of 3-HP-producing chassis by exploiting metabolic regulation, controlling carbon flux, balancing cofactor generation, and optimizing fermentation conditions. First, the malonyl-CoA (MCA) pathway was recruited and rebalanced in Escherichia coli . Subsequently, a hybrid pathway integrating the Embden-Meyerhof-Parnas pathway with the nonoxidative glycolysis pathway was systematically modulated to enhance carbon flux to the MCA pathway, followed by fine-tuning NADPH regeneration. Then, by optimizing the fermentation conditions, 3-HP production was significantly improved, reaching 6.8 g/L. Finally, in a fed-batch experiment, the final chassis produced 42.8 g/L 3-HP, corresponding to a 0.4 mol/mol yield and 0.6 g/(L·h) productivity.

Cadmium (Cd) in rice is a significant concern for its quality and safety. Currently, there is a crucial need to develop cost-effective and efficient ways to remove Cd or re-utilize Cd-contaminated rice. The food additive sodium erythorbate is produced via 2-ketogluconic acid (2KGA) fermentation by Pseudomonas plecoglossicida and lactonization using starch-rich raw materials, such as rice. We aimed to determine whether cadmium-contaminated rice can be used to produce sodium erythorbate. To achieve this aim, the migration of cadmium during the production of sodium erythorbate from Cd-contaminated rice was studied. Five rice varieties with different Cd contents from 0.10 to 0.68 mg/kg were used as raw materials. The results indicated the presence of Cd in rice and CaCO 3 did not have a notable impact on the fermentation performance of 2KGA. The acidification of 2KGA fermentation broth, the addition of K 4 Fe(CN) 6 ·3H 2 O and ZnSO 4 , and 2KGA purification using cation exchange effectively removed >98% of the Cd in the fermentation broth, but the 2KGA yield remained high at approximately 94%. The sodium erythorbate synthesized from Cd-contaminated rice was of high quality and free from Cd, meeting the requirements of the Chinese National Standard, GB 1886.28-2016. The study provided a safe and effective strategy for comprehensively utilizing Cd-contaminated rice to produce high value-added food additive., Competing Interests: Declaration of competing interest The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper., (Copyright © 2024 Elsevier Ltd. All rights reserved.)

2-Keto-D-gluconic acid (2KGA) is mainly used for industrial production of erythorbic acid, a food antioxidant. In this study, a 2KGA producing strain JUIM02 was firstly identified as Arthrobacter globiformis by morphological observation and 16S rDNA sequencing. The 2KGA synthetic capacity of A. globiformis JUIM02 was evaluated by both fermentation and bioconversion, with 180 g/L dextrose monohydrate as substrates, in shake flasks and 5 L fermenters. For fermentation, 2KGA titer, yield, molar yield, and productivity of JUIM02 reached 159.05 g/L, 0.97 g/g, 90.18%, and 6.63 g/L/h in 24 h. For non-sterile and buffer-free bioconversion by free resting cells (~ 3.2 g/L dry cell weight) of JUIM02, these data were 172.96 g/L, 1.06 g/g, 98.07%, and 5.41 g/L/h in 32 h. Moreover, JUIM02 resting cells could be repeatedly used. Resting cells stored at 4 °C within 30 days showed stable bioconversion capacity, with 2KGA titers ≥ 171.50 g/L, yields ≥ 1.04 g/g, and molar yields ≥ 97.24%. The 2KGA synthetic pathway in A. globiformis, which was rarely reported, was also speculated similar to Pseudomonas and verified preliminarily. In conclusion, A. globiformis JUIM02 is a promising 2KGA industrial-producing strain suitable for various production methods and a suitable object for 2KGA metabolism research of A. globiformis.

A new strain producing high yield of D-arabitol was isolated from hyperosmotic environments and the ITS rDNA sequencing analysis revealed it as Zygosaccharomyces rouxii. In addition, using a pH control and repeated-batch fermentation strategy in a 5-L reactor, the maximum yield and the highest volumetric productivity of D-arabitol were 93.48 ± 2.79 g/L and 1.143 g/L h, respectively. Volumetric productivity was successfully improved from 0.86 to 1.143 g/L h, which was increased by 32.9 % after 72 h of fermentation. Z. rouxii JM-C46 has potential to be used for D-arabitol and xylitol production from glucose via D-arabitol route.

Food matrix plays an important role in regulating macronutrient digestibility. In this study, lactic acid bacteria (LAB)-fermented soy protein isolates (FSPIs) were prepared at a series of concentration (0.2%–5.0%, w/v). FSPIs with varied structures were obtained and tested in an in vitro dynamic gastrointestinal model. Then, a comparative digestomics research was conducted. Results demonstrated that the lowest gelation concentration of soy protein during LAB fermentation was 1.9% (w/v). The FSPIs showed structures ranging from a loosely stacked layer (non-gel, NG) to a denser gel network with varied hardness (weak gel, WG; medium gel, MG; and firm gel, FG) when the protein concentration was adjusted. The protein profile of gastrointestinal digestates demonstrated higher soluble protein and peptide in FSPI gels compared with FSPI-NG. FSPI gel digestates were predominantly promoted in glycinin G1 and the β-conglycinin α subunit. The change was dynamic between FSPI gels with varied structures. Weaker gels (FSPI-WG and FSPI-MG) facilitated the hydrolysis of glycinin G1/G4 and β-conglycinin α/β subunits at early and medium digestions (0–30 min). In comparison, the firmer gel (FSPI-FG) showed a postponed but more extensive promotion of the degradation of glycinin G1/G2 and β-conglycinin α subunits at the late digestion (180 min). The spatial structures of glycinin G1 and β-conglycinin α subunits demonstrated variations in seven and eight regions, respectively. Glycinin's region 6 (Y 374 –R 388) and β-conglycinin's region 7 (L 491 –T 519), which are located at the interior of the 3D structure, were the key regions contributing to the discrepancies. [Display omitted] • The lowest gelation concentration was 1.9% (w/v) for fermented soy protein gel. • Higher protein concentration allowed the formation of denser gel network. • Fermented soy protein gel had intestinal digestate with higher peptidome abundance. • Gel at higher protein concentration showed a postponed but extensive hydrolysis. • Gelation promoted the proteolysis of interior region of glycinin and β-conglycinin. [ABSTRACT FROM AUTHOR]

D-Ribose is a five-carbon sugar and generally used as an energy source to improve athletic performance and the ability. The culture conditions for maximum D-ribose production performance from cheap raw material corn starch hydrolysate were improved by using one-factor-at-a-time experiments and a three-level Box-Behnken factorial design. The optimal fermentation parameters were obtained as 36°C culture temperature, 10% inoculum volume, and 7.0 initial pH. The mathematical model was then developed to show the effect of each medium composition and their interactions on the production of D-ribose and estimated that the optimized D-ribose production performance with the concentration of 62.13 g/L, yield of 0.40 g/g, and volumetric productivity of 0.86 g/L·h could be obtained when the medium compositions were set as 157 g/L glucose, 21 g/L corn steep liquor, 3.2 g/L (NH4)2SO4, 1 g/L yeast extract, 0.05 g/L MnSO4·H2O, and 20 g/L CaCO3. These findings indicated the D-ribose production performance was significantly improved compared to that under original conditions. [ABSTRACT FROM AUTHOR]

A non-sterile and buffer-free 2-keto-gluconic acid (2KGA) production method was proposed by using resting cells from an industrial strain of Pseudomonas fluorescens AR4. 2KGA achieved a maximum production performance of 195.00 g/L, which corresponded to 3.05 g/L h of total productivity and 1.07 g/g of yield under optimal conditions, including resting cell aged 20 h, a cell concentration of 3.0 g/L, a reaction temperature of 30 °C, a glucose concentration of 181.82 g/L, and a reaction volume of 20 mL during the 64-h bioconversion process. P. fluorescens AR4 resting cells showed stable bioconversion activity after reuse 3 times or storage for less than 28 d at 4 °C. These findings suggested that the proposed non-sterile and buffer-free bioconversion of glucose to 2KGA using P. fluorescens AR4 resting cells had remarkable advantages, including ease handling and low cost, and they are a potent application for industrial production of 2KGA. [ABSTRACT FROM AUTHOR]

2-Ketogluconate (2KGA) is an organic acid that is important for pharmaceutical, cosmetic, and environmental applications. Pseudomonas plecoglossicida JUIM01 strain is an important industrial 2KGA producer in China. In this paper, we found that P. plecoglossicida JUIM01 could convert glucose to 2KGA extracellularly, and the formed 2KGA was subsequently consumed after glucose was exhausted during the fermentation process. Experiments of glucose and 2KGA supplementation during fermentation process revealed that, only when glucose was exhausted, the strain started to consume the product 2KGA. Then, the mechanism of this phenomenon was investigated at transcription and protein levels, and the results indicated that P. plecoglossicida JUIM01 possesses carbon catabolite repression of 2KGA metabolism by glucose. Next, increasing the supply of glucose could attenuate 2KGA consumption and enhance the 2KGA yield from glucose. Finally, fed-batch fermentation of P. plecoglossicida JUIM01 resulted in 205.67 g/L of 2KGA with a productivity of 6.86 g/L/h and yield of 0.953 g/g glucose. These results can provide references for the industrial fermentation production of 2KGA and other fermentation products. [ABSTRACT FROM AUTHOR]