Cost-effective optimization of gellan gum production by Sphingomonas paucimobilis using corn steep liquor

Abstract

Gellan gum, produced by Sphingomonas paucimobilis, is increasingly used in food and pharmaceutical industries as stabilizing, emulsifying, texturing and gelling agents. However, its high production costs may limit its full commercial potential. Therefore, in this study, we investigated ways to reduce gellan gum production costs and improve yields. We first revealed corn steep liquor (CSL) as a cost-effective nutrient source that can improve gellan gum yields. We then systematically optimized culture conditions even further, and revealed that the addition of Triton X-100 surfactant and selected inorganic nitrogen sources improved gellan gum production. Under our optimized conditions (glucose 33.75?g/L, CSL 10?g/L, urea 2.5?g/L, MgSO₄ 1.08?g/L, KH₂PO₄ 3.24?g/L, K₂SO₄ 1?g/L and Triton X-100 0.75?g/L), we yielded a maximum concentration of 14.41?g/L, which was about 1.5-fold higher than non-optimized CSL-based medium. Our findings highlight the use of CSL as a cost effective and promising nutrient source for industrial production of gellan gum.     

The production of bioflocculants by Bacillus licheniformis using molasses and its application in the sugarcane industry

A bioflocculant produced by B. licheniformis was investigated with regard to a low-cost culture medium and its industrial application. Molasses replaced sucrose as the sole carbon source in bioflocculant fermentation. The optimum low-cost culture medium was determined to be composed of 20 g/L molasses, 0.4 g/L urea, 0.4 g/L NaCl, 0.2 g/L KH₂PO₄, 1.6 g/L K₂HPO₄, and 0.2 g/L MgSO₄. The bioflocculant from B. licheniformis was then applied to treat sugarcane-neutralizing juice to remove colloids, suspended particles, and coloring matters in a sugar refinery factory. The optimal operation conditions were a bioflocculant dosage of 21 U/mL, pH 7.3 and a heating temperature of 100°C. The color and turbidity of the sugarcane juice reached IU 1267 and IU 206, respectively, after clarification with the bioflocculant; these values were almost the same as those acquired following treatment with polyacrylamide (PAM), the most widely applied flocculant in sugar industries. These results suggest the great potential for use of bioflocculants in the sugar refinery process.     

Enhanced curdlan production in <Emphasis Type="Italic">Agrobacterium</Emphasis> sp. ATCC 31749 by addition of low-polyphosphates

A large amount of adenosine triphosphate with high energy phosphate bonds is required for uridine triphosphate regeneration during curdlan biosynthesis by Agrobacterium sp. ATCC 31749. To supply high energy for curdlan synthesis, three low-polyphosphates (Na₄P₂O₇, Na₅P₃O₁₀, and (NaPO₃)₆) with higher energy phosphate bonds were employed to substitute for KH₂PO₄-K₂HPO₄ in fermentation medium. Two genes encoding the polyphosphate metabolizing enzymes, polyphosphate kinase and exopolyphosphatase, were amplified and showed 95% homology to those in Agrobacterium sp. C58 by sequence analysis. The curdlan yields were enhanced by 23 and 134% when phosphate concentrations 0.024 mol/L of Na₅P₃O₁₀ and 0.048 mol/L of (NaPO₃)₆ respectively, were added in the medium. The maximum curdlan yield of 30 ± 1.02 g/L was obtained with the addition of 0.048 mol/L of (NaPO₃)₆ with 5 g/L CaCO₃ in the medium. When CaCO₃ was removed from the culture and the three lowpolyphosphates were added, the pH and biomass yield dropped remarkably and little or no curdlan was produced. The culture containing 0.048 mol/L of (NaPO₃)₆ was mixed with KH₂PO₄-K₂HPO₄ and CaCO₃ in the medium, but showed no effect on curdlan production. However, curdlan yield was improved by 49 ∼ 60% when CaCO₃ was removed from the medium and KH₂PO₄-K₂HPO₄ acted as a buffer. It appears that the positive effect of (NaPO₃)₆ on curdlan production required the buffering capacity of CaCO₃ and the absence of KH₂PO₄-K₂HPO₄ competing as a phosphate supplier.     

<Emphasis Type="Italic">Bacillus amyloliquefaciens</Emphasis> Spore Production Under Solid-State Fermentation of Lignocellulosic Residues

This study was conducted to elucidate cultivation conditions determining Bacillus amyloliquefaciens B-1895 growth and enhanced spore formation during the solid-state fermentation (SSF) of agro-industrial lignocellulosic biomasses. Among the tested growth substrates, corncobs provided the highest yield of spores (47?×?10¹⁰ spores g^?1 biomass) while the mushroom spent substrate and sunflower oil mill appeared to be poor growth substrates for spore formation. Maximum spore yield (82?×?10¹⁰ spores g^?1 biomass) was achieved when 15 g corncobs were moistened with 60 ml of the optimized nutrient medium containing 10 g peptone, 2 g KH₂PO₄, 1 g MgSO₄·7H₂O, and 1 g NaCl per 1 l of distilled water. The cheese whey usage for wetting of lignocellulosic substrate instead water promoted spore formation and increased the spore number to 105?×?10¹⁰ spores g^?1. Addition to the cheese whey of optimized medium components favored sporulation process. The feasibility of developed medium and strategy was shown in scaled up SSF of corncobs in polypropylene bags since yield of 10?×?10¹¹ spores per gram of dry biomass was achieved. In the SSF of lignocellulose, B. amyloliquefaciens B-1895 secreted comparatively high cellulase and xylanase activities to ensure good growth of the bacterial culture.     

Optimization of chitinase production by a new <Emphasis Type="Italic">Streptomyces griseorubens</Emphasis> C9 isolate using response surface methodology

The purpose of this article is to use statistical Plackett–Burman and Box–Wilson response surface methodology to optimize the medium components and, thus, improve chitinase production by Streptomyces griseorubens C9. This strain was previously isolated and identified from a semi-arid soil of Laghouat region (Algeria). First, syrup of date, colloidal chitin, yeast extract and K₂HPO₄, KH₂PO₄ were proved to have significant effects on chitinase activity using the Plackett–Burman design. Then, an optimal medium was obtained by a Box–Wilson factorial design of response surface methodology in liquid culture. Maximum chitinase production was predicted in medium containing 2% colloidal chitin, 0.47% syrup of date, 0.25 g/l yeast extract and 1.81 g/l K₂HPO₄, KH₂PO₄ using response surface plots of the STATISTICA software v.12.0.     

Structures and Properties of Gellan Polymers Produced by Sphingomonas paucimobilis ATCC 31461 from Lactose Compared with Those Produced from Glucose and from Cheese Whey

The dairy industry produces large quantities of whey as a by-product of cheese production and is increasingly looking for new ways to utilize this waste product. Gellan gum is reliably produced by Sphingomonas paucimobilis in growth media containing lactose, a significant component of cheese whey, as a carbon source. We studied and compared polysaccharide biosynthesis by S. paucimobilis ATCC 31461 in media containing glucose, lactose (5 to 30 g/liter), and sweet cheese whey. We found that altering the growth medium can markedly affect the polysaccharide yield, acyl substitution level, polymer rheological properties, and susceptibility to degradation. Depression of gellan production from lactose compared with gellan production from glucose (approximately 30%) did not appear to occur at the level of synthesis of sugar nucleotides, which are the donors of monomers used for biosynthesis of the repetitive tetrasaccharide unit of gellan. The lactose-derived biopolymer had the highest total acyl content; the glucose- and whey-derived gellans had similar total acyl contents but differed markedly in their acetate and glycerate levels. Rheological studies revealed how the functionality of a gellan polysaccharide is affected by changes in the acyl substitution.     

IMPROVED Candida methylica FORMATE DEHYDROGENASE FERMENTATION THROUGH STATISTICAL OPTIMIZATION OF LOW-COST CULTURE MEDIA

NAD⁺-dependent formate dehydrogenase (FDH, EC 1.2.1.2) is of use in the regeneration of NAD(P)H coenzymes, and therefore has strong potential for practical application in chemical and medical industries. A low-cost production of recombinant Escherichia coli (E. coli) containing FDH from Candida methylica (cmFDH) was optimized in molasses-based medium by using response surface methodology (RSM) based on central composite design (CCD). The beet molasses as a sole carbon source, (NH₄)₂HPO₄ as a nitrogen and phosphorus source, KH₂PO₄ as a buffer agent, and Mg₂SO₄ · 7H₂O as a magnesium and sulfur source were used as variables in the medium. The optimum medium composition was found to be 34.694 g L^?1 of reducing sugar (equivalent to molasses solution), 8.536 g L^?1 of (NH₄)₂HPO₄, 3.073 g L^?1 of KH₂PO₄, and 1.707 g L^?1 of Mg₂SO₄ · 7H₂O. Molasses-based culture medium increased the yield of cmFDH about three times compared to LB medium. The currently developed media has the potential to be used in industrial bioprocesses with low-cost production.     

Co-fermentation of cassava waste pulp hydrolysate with molasses to ethanol for economic optimization

Cassava waste pulp (CWP)–enzymatic hydrolysate was co-fermented with molasses (CWP-EH/molasses mixture) with the aim to optimize ethanol production by Saccharomyces cerevisiae TISTR 5606 (SC 90). The optimal fermentation conditions for ethanol production using this mixture were 245 g/L initial total sugar supplemented with KH₂PO₄ (8 g/L), at 30 °C for 48 h of fermentation under an oxygen-limited condition with agitation at 100 rpm, producing an ethanol concentration of 70.60 g/L (0.31 g ethanol/g total sugar). The addition of cassava tuber fiber (solid residue of CWP after enzymatic hydrolysis) at 30 g/L dry weight to the CWP-EH/molasses mixture increased ethanol production to 74.36 g/L (0.32 g ethanol/g total sugar). Co-fermentation of CWP-EH with molasses had the advantage of not requiring any supplementation of the fermentation mixture with reduced nitrogen.     

Screening of lipid high producing mutant from rhodotorula glutinis by low ion implantation and study on optimization of fermentation medium

In order to obtain lipid producing strain with high-yield, the wild type stain Rhodotorula glutinis was treated by low ion implantation, and optimization of fermentation medium for higher lipid yield was carried out using mutant strain. It was found that the strain had a higher positive mutation rate when the output power was 10 keV and the dose of N⁺ implantation was 80 × 2.6 × 10¹³ ions/cm². Then a high-yield mutant strain D30 was obtained through cid-heating coupling ultrasonic method and lipid yield was 3.10 g/L. Additionally, the surface response method was used to optimize fermentation medium. The three significant factors (glucose, peptone, KH₂PO₄) were optimized using response surface methodology (RSM), and the optimized parameters of fermentation medium were as follows: glucose 73.40 g/L, peptone 1.06 g/L and KH₂PO₄ 3.56 g/L. Finally the fermentation characteristic of high-yield mutation strain D30 was studied, when fermentation time was 10 days, which lipid yield increased to 7.81 g/L. Fatty acid composition of the lipid was determined by GC, and the most represented fatty acids of mutant D30 were C16:0 (11.4 %), C16:1 (5.66 %), C18:1 (49.3 %), and C18:2 (27.0 %).     

Optimization of polyhydroxybutyrate production by <Emphasis Type="Italic">Bacillus</Emphasis> sp. CFR 256 with corn steep liquor as a nitrogen source

Polyhydroxyalkanotes (PHAs), the eco-friendly biopolymers produced by many bacteria, are gaining importance in curtailing the environmental pollution by replacing the non-biodegradable plastics derived from petroleum. The present study was carried out to economize the polyhydroxybutyrate (PHB) production by optimizing the fermentation medium using corn steep liquor (CSL), a by-product of starch processing industry, as a cheap nitrogen source, by Bacillus sp. CFR 256. Response surface methodology (RSM) was used to optimize the fermentation medium using the variables such as corn steep liquor (5–25 g l⁻¹), Na₂HPO₄ 2H₂O (2.2–6.2 g l⁻¹), KH₂PO₄ (0.5–2.5 g l⁻¹), sucrose (5–55 g l⁻¹) and inoculum concentration (1–25 ml l⁻¹). Central composite rotatable design (CCRD) experiments were carried out to study the complex interactions of the variables. The optimum conditions for maximum PHB production were (g l⁻¹): CSL-25, Na₂HPO₄ 2H₂O-2.2, KH₂PO₄ − 0.5, sucrose − 55 and inoculum − 10 (ml l⁻¹). After 72 h of fermentation, the amount of PHA produced was 8.20 g l⁻¹ (51.20% of dry cell biomass). It is the first report on optimization of fermentation medium using CSL as a nitrogen source, for PHB production by Bacillus sp.     

Statistical media optimization for growth and PHB production from methanol by a methylotrophic bacterium

Media components were optimized by statistical design for cell growth and PHB production of Methylobacterium extorquens DSMZ 1340. Four important components of growth media were optimized by central composite design. The growth increased from an OD = 1.35 for Choi medium as control to an OD = 2.15 for optimal medium. Then media components for PHB production were optimized. Optimization of five important factors was conducted by response surface method. The optimal composition of PHB production medium was found to be at 7.8 (g/L) Na₂HPO₄ · 12H₂O, and surprisingly at zero concentration of (NH₄)₂SO₄, KH₂PO₄, MgSO₄ and MnSO₄. The PHB production was found to be 2.95 (g/L) at this medium. RSM results indicated that a deficiency of nitrogen and magnesium is crucial for PHB accumulation in this microorganism. Also, PHB production was carried out in a 5 L fermentor at the optimum condition which resulted in 9.5 g/L PHB and 15.4 g/L cell dry weight with 62.3% polymer content.     

Evaluation of different culture conditions ofClostridium bifermentans DPH-1 for cost effective PCE degradation

Clostridium bifermentans strain DPH-1 has already been found to dechlorinate perchloroethylene (PCE) tocis-dichloroethylene (cis-DCE)via trichloroethylene (TCE). In this study, our investigation on different culture conditions of this DPH-1 strain was extended to find a more efficient and cost effective growth medium composition for this DPH-1 strain in bioremediation practices. Temperature dependency of strain DPH-1 showed that the growth starting time and PCE degradation at 15°C was very slow compared to that of 30°C, but complete PCE degradation occurred in both cases. For the proper utilization of strain DPH-1 in more cost effective bioremediation practices, a simpler composition of an effective media was studied. One component of the culture medium, yeast extract, had been substituted by molasses, which served as a good source of electron donor. The DPH-1 strain in the medium containing molasses, in the presence of K₂HPO₄ and KH₂PO₄, showed identical bacterial multiplication (0.135 mg protein mL⁻¹h⁻¹) and PCE degradation rates (0.38 μM/h) to those of the yeast extract containing medium.     

Determination of the best nutrient medium for the production of L-lactic acid from beet molasses a statistical approach

Optimization studies have been carried out for the production of L-lactic acid from the fermentation of beet molasses by Lactobacillus delbrueckii. A PLACKETT -BURMAN Design and a Central Composite Design have been used to determine the most suitable nutrient medium for obtaining a maximum cell concentration. A second-order polynomial empirical model relating both the cell and nutrient concentrations was formulated. The variables selected for the study were Yeast Extract, Peptone, Tween 80 (antifoam), MgSO₄ · 7H₂O, MnSO₄·4H₂O, FeSO₄ · 7H₂O and K₂HPO₄/KH₂PO₄. Among them, only Yeast Extract and Peptone were found to significantly affect the cell concentration. A maximum cell yield was found when the concentrations of Yeast Extract and Peptone were, respectively, 5.31 g/l and 5.08 g/l. All conclusions are restricted to the experimental range studied.     

Isolation of a feather-degrading strain of bacterium from spider gut and the purification and identification of its three key enzymes

A novel feather-degrading bacterium named CA-1 was isolated from the gut of the spider Chilobrachys guangxiensis, which degrades native whole chicken feathers within 20 h. The CA-1 was confirmed to belong to Stenotrophomonas maltophilia based on morphologic and molecular analysis. Maximum feather degradation activity of the bacterium was observed at 37 °C in basal feather medium (NaCl 0.5 g/L, KH₂PO₄ 0.3 g/L, K₂HPO₄ 0.4 g/L, feather powder 10.0 g/L, pH 8.0), which was inhibited when glucose and ammonium nitrate were added in the medium. Furthermore, the purified enzymes under the optimal and suppressive conditions were analyzed respectively by SDS-PAGE and LC–MS/MS. Three enzymes, namely alkaline serine protease (29.1 kDa), ABC transporter permease (27.5 kDa), and alkaline phosphatase (40.8 kDa), were isolated and identified from the supernatant of the optimal culture and were considered to play principal roles. On the other hand, the potential synergic effects of the three proteins in S. maltophilia CA-1 feather degradation system were analyzed theoretically. CA-1 may product outer-membrane vesicles comprised of membranes and periplasmic proteins in the feather medium. The newly identified CA-1 and its synergic enzymes provide a new insight into further understanding the molecular mechanism of feather degradation by microbes. They also have potential application in cost-effectively degrading feathers into feeds and fertilizers through careful optimization and engineering of the three newly identified enzymes.     

Acetone and Butanol Production by Clostridium acetobutylicum in a Synthetic Medium

The effect of the component concentrations of a synthetic medium on acetone and butanol fermentation by Clostridium acetobutylicum ATCC 824 was investigated. Cell growth was dependent on the presence of Mg, Fe, and K in the medium. Mg and Mn had deleterious effects when in excess. Ammonium acetate in excess caused acid fermentation. The metabolism was composed of two phases: an acid phase and a solvent one. Low concentrations of glucose allowed the first phase only. The theoretical ratio of the conversion of glucose to solvents, which was 28 to 33%, was obtained with the following medium: MgSO₄, 50 to 200 mg/liter; MnSO₄, 0 to 20 mg/liter; KCl, 0.015 to 8 g/liter (an equivalent concentration of K⁺ was supplied in the form of KH₂PO₄ and K₂HPO₄); FeSO₄, 1 to 50 mg/liter; ammonium acetate, 1.1 to 2.2 g/liter; para-aminobenzoic acid, 1 mg/liter; biotin, 0.01 mg/liter; glucose, 20 to 60 g/liter.     

Aqueous two-phase extraction coupled with ultrafiltration for purification of amyloglucosidase

Aqueous two phase extraction (ATPE) in combination with ultrafiltration was employed for concentration and purification of amyloglucosidase produced by solid state fermentation. After extraction (with water) from dry moldy bran the dilute enzyme extract was concentrated by ATPE in a polyethylene glycol (PEG)/maltodextrin (MDX) system. The enzyme in the top PEG rich phase was then extracted into a Na₂HPO₄ rich bottom phase and further concentrated by ultrafiltration. The partitioning behavior of amyloglucosidase was examined in PEG/MDX, PEG/Na₂SO₄, PEG/Na₂HPO₄, PEG/KH₂PO₄ aqueous two phase systems. Effect of buffering salts such as NaCl, Na₂HPO₄, KH₂PO₄ and Na₂SO₄ on the partitioning behavior of enzyme was studied in PEG/MDX system. Maximum partitioning of amyloglucosidase was seen with KH₂PO₄ (m = 18.1). A two stage ATPE employing PEG/MDX (buffered with KH₂PO₄) and PEG/Na₂HPO₄ systems, followed by ultrafiltration has resulted in an overall recovery of 78.4% with 3.1 fold purification and 9.4 fold concentration of the enzyme.     

Impact of phosphate concentration on docosahexaenoic acid production and related enzyme activities in fermentation of Schizochytrium sp.

Docosahexaenoic acid (DHA) is an important and widely used infant food additive. In this study, the effects of phosphate concentration on lipid and especially DHA synthesis in the oleaginous fungi Schizochytrium sp. HX-308 have been investigated in batch cultures. The maximum DHA yield (8.9 g/L) and DHA productivity (148.3 mg/L h) in 0.1 g/L KH₂PO₄ concentration were higher than the DHA yield (6.2 g/L) and DHA productivity (86.1 mg/L h) in 4 g/L KH₂PO₄ concentration. Furthermore, differences in related enzyme activities (malic enzyme, glucose-6-phosphate dehydrogenase and NAD⁺-isocitrate dehydrogenase) between phosphate-sufficient and phosphate-limitation conditions were assayed. The results showed that the phosphate-limitation condition could maintain higher activities of malic enzyme and glucose-6-phosphate dehydrogenase in addition to lower activity of NAD⁺-isocitrate dehydrogenase. In addition, glucose-6-phosphate dehydrogenase might be the main supplier of NADPH at the early stage of fermentation while malic enzyme might be the provider at the late stage. This information might explain the regulation mechanism of phosphate limitation for lipid production and be useful for further DHA production enhancement.     

Optimization of <Emphasis Type="Italic">Verticillium lecanii</Emphasis> spore production in solid-state fermentation on sugarcane bagasse

Verticillium lecanii is an entomopathogen with high potential in biological control of pests. We developed a solid-state fermentation with sugarcane bagasse as carrier absorbing liquid medium to propagate V. lecanii spores. Using statistical experimental design, we optimized the medium composition for spore production. We first used one-factor-at-a-time design to identify corn flour and yeast extract as the best carbon and nitrogen sources for the spore production of V. lecanii. Then, we used two-level fractional factorial design to confirm corn flour, yeast extract, and KH₂PO₄ as important factors significantly affecting V. lecanii spore production. Finally, we optimized these selected variables using a central composite design and response surface method. The optimal medium composition was (grams per liter): corn flour 35.79, yeast 8.69, KH₂PO₄ 1.63, K₂HPO₄ 0.325, and MgSO₄ 0.325. Under optimal conditions, spore production reached 1.1 × 10¹⁰ spores/g dried carrier, much higher than that on wheat bran (1.7 × 10⁹ spores/g initial dry matter).     

Rosmarinic acid by Lavandula vera MM cell suspension: Phosphorus effect

Summary The growth of Lavandula vera MM cell suspension and biosynthesis of rosmarinic acid were followed during its cultivation in Linsmayer - Skoog (LS) medium (containing 170 mg/L KH₂PO₄, control cultivation) and in modified LS media, containing different concentration of KH₂PO₄. Doubled concentration of KH₂PO₄ (340 mg/L) caused an increase in the amount of biosynthesised cell biomass (17 g/L vs 13 g/L for control cultivation) and rosmarinic acid (140 mg/L vs 68 mg/L for control cultivation).