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.     

Statistical optimization of medium composition for bacterial cellulose production by Gluconacetobacter hansenii UAC09 using coffee cherry husk extract--an agro-industry waste

During the production of grape wine, the formation of thick leathery pellicle/bacterial cellulose (BC) at the airliquid interface was due to the bacterium, which was isolated and identified as Gluconacetobacter hansenii UAC09. Cultural conditions for bacterial cellulose production from G. hansenii UAC09 were optimized by central composite rotatable experimental design. To economize the BC production, coffee cherry husk (CCH) extract and corn steep liquor (CSL) were used as less expensive sources of carbon and nitrogen, respectively. CCH and CSL are byproducts from the coffee processing and starch processing industry, respectively. The interactions between pH (4.5- 8.5), CSL (2-10%), alcohol (0.5-2%), acetic acid (0.5- 2%), and water dilution rate to CCH ratio (1:1 to 1:5) were studied using response surface methodology. The optimum conditions for maximum BC production were pH (6.64), CSL (10%), alcohol (0.5%), acetic acid (1.13%), and water to CCH ratio (1:1). After 2 weeks of fermentation, the amount of BC produced was 6.24 g/l. This yield was comparable to the predicted value of 6.09 g/l. This is the first report on the optimization of the fermentation medium by RSM using CCH extract as the carbon source for BC production by G. hansenii UAC09.     

Sclerotia growth and carotenoid production of Penicillium sp PT95 during solid state fermentation of corn meal

Using corn meal as fermentation substrate, the effect of some factors, fermentation time and supplementation of saccharide and nitrogen sources as well as vegetable oil, on the sclerotia growth and carotenoid production of Penicillium sp PT95 during solid state fermentation were studied. When PT95 strain was grown on the amended medium by supplementing of 3g NaNO3, 10g maltose and 2.5g soybean oil per liter of salt solution to basal medium for 20 days, the dry sclerotia weight and carotenoid yield reached 9.70 g and 5260 g / 100 g of substrate, respectively. Without supplementation only 5.36g dry sclerotia and 2149g carotenoid / 100 g of substrate was attained. © Rapid Science Ltd. 1998     

A factorial approach for a sugarcane juice-based low cost culture medium: increasing the astaxanthin production by the red yeast Phaffia rhodozyma

A sugarcane juice-based low cost culture medium was previously explored to produce the carotenoid pigment astaxanthin in liquid culture by the red yeast Phaffia rhodozyma (1300?μg astaxanthin/g of dry yeast and 6500?μg/l whole culture medium). Two peculiar limitations in Phaffia are growth temperature (<26?°C) and lack of sugar osmotolerance. Two advantages are the wide biochemical ability for the assimilation and metabolization of disaccharides and the prompt utilization of simple nitrogen sources. For instance, the sucrolytic/ureolytic enzymatic activities deserves exploration. In order to improve the culture medium composition and the conditions of fermentation for highly oxygenated carotenoids (e.g., astaxanthin) a study was carried out with a factorial design in two steps. As a first step, the production of astaxanthin was studied as a function of the nutrient concentration levels and their interactions. The production increase (μg/l) obtained was 23.0% but at the expense of 16.0% pigment content decrease (μg/g). In the second step, the variables pH and agitation level (OTR, oxygen transfer rate) were optimized and then, both goals were attained: the increase of pigment content (418?μg astaxanthin/g of yeast) as well as the absolute pigment production enhancement (1987?μg/l).     

Fermentative production of succinic acid from glucose and corn steep liquor byAnaerobiospirillum succiniciproducens

Anaerobiospirillum succiniciproducens requires expensive complex nitrogen sources such as yeast extract and polypeptone for its growth and succinic acid production. It was found thatA. succiniciproducens was able to grow in a minimal medium containing glucose when supplemented with corn steep liquor (CSL) as the sole complex nitrogen source. The concentration of CSL had a significant effect on the glucose consumption byA. succiniciproducens. When 10–15 g/L of CSL was supplemented, cells were grown to an OD₆₆₀ of 3.5 and produced 17.8 g/L succinic acid with 20 g/L glucose. These results are similar to those obtained by supplementing yeast extract and polypeptone, thereby suggesting that succinic acid can be produced more economically using glucose and CSL.     

玉米浆对Vc二步发酵产2-酮基-L-古龙酸影响的研究

通过在培养基中添加不同量的玉米浆,研究其对氧化葡萄糖酸杆菌（俗称小菌）生产Vc前体2-酮基-L-古龙酸的影响,并研究玉米浆成分中的12种主要氨基酸对小菌产酸的影响。结果表明：每100 mL发酵培养基中添加2.5 g左右过滤除菌玉米浆时,2-酮基-L-古龙酸产量高达26.84 mg/mL,小菌活菌数为不添加玉米浆时小菌单菌发酵下的9.74倍。过量玉米浆抑制小菌产酸。12种氨基酸单独与氧化葡萄糖酸杆菌发酵培养及全部混合后与氧化葡萄糖酸杆菌发酵培养对产酸及菌体生长无影响。     

Effect of corn steep liquor on xanthan production by Xanthomonas campestris

Summary The addition of corn steep liquor (CSL) to batch cultures of Xanthomonas campestris using sucrose as carbon source stimulated cell growth rate, viscosity and xanthan production as compared to non-supplemented cultures. The addition of CSL to a basal medium at a dose of 1 g/l, increased xanthan production and viscosity by 22% and 44% respectively. CSL also shortened the cultivation time and promoted a more efficient sucrose utilization for polymer synthesis. After 72 h of incubation the xanthan yield per sucrose consumed in the CSL-amended culture was 0.63 g/g, this is, 15% higher than without CSL addition. At higher doses of CSL cell growth rate was also increased but not polymer production.     

Statistical optimization of a culture medium for biomass and poly(3-hydroxybutyrate) production by a recombinant Escherichia coli strain using agroindustrial byproducts.

A statistically based Plackett-Burman screening design identified milk whey and corn steep liquor concentrations as well as ionic strength (based on phosphate buffer concentration) as the three main independent components of the culture medium that significantly (p < 0.05) influenced biomass and poly(3-hydroxybutyrate) (PHB) production in recombinant cells of Escherichia coli. This strain carries a plasmid encoding phb genes from a natural isolate of Azotobacter sp. Response surface methodology, using a central composite rotatable design, demonstrated that the optimal concentrations of the three components, defined as those yielding maximal biomass and PHB production in shaken flasks, were 37.96 g deproteinated milk whey powder/l, 29.39 g corn steep liquor/l, and 23.76 g phosphates/l (r2 = 0.957). The model was validated by culturing the recombinant cells in medium containing these optimal concentrations, which yielded 9.41 g biomass/l and 6.12 g PHB/l in the culture broth. Similar amounts of PHB were obtained following batch fermentations in a bioreactor. These results show that PHB can be produced efficiently by culturing the recombinant strain in medium containing cheap carbon and nitrogen sources.     

Effects of pH and corn steep liquor variability on mannitol production by Lactobacillus intermedius NRRL B-3693

Lactobacillus intermedius NRRL B-3693 produced mannitol, lactic acid, and acetic acid when grown on fructose at 37°C. The optimal pH for mannitol production from fructose by the heterofermentative lactic acid bacterium (LAB) in pH-controlled fermentation was at pH 5.0. It produced 160.7 ± 1.1 g mannitol in 40 h with a volumetric productivity of 4.0 g l⁻¹ h⁻¹ in a simplified medium containing 250 g fructose, 50 g corn steep liquor (CSL), and 33 mg MnSO₄ per liter. However, the mannitol production by the LAB was severely affected by the variability of CSL. The supplementation of CSL with soy peptone (5 g/l), tryptophan (50 mg/l), tryptophan (50 mg/l) plus tyrosine (50 mg/l), or commercial protease preparation (2 ml/100 g of CSL) enhanced the performance of the inferior CSL and thus helped to overcome the nutrient limitations.     

Increased production of bacteriocin ST4SA byEnterococcus mundtii ST4SA in modified corn steep liquor

Enterococcus mundtii ST4SA produces a broad-spectrum bacteriocin (bacST4SA), active against Gram-positive and Gramnegative bacteria. Growth in corn steep liquor (CSL) with a sugar content of 5.0 and 10.0 g/l yielded bacST4SA levels of 12800 AU/ml. A four-fold increase in bacST4SA production (51200 AU/ml) was recorded in CSL with a sugar content of 7.5 g/l supplemented with 6.5 g/l yeast extract (CSL-YE). Poor growth and low levels of bacST4SA production were observed when cells were grown in CSL-YE controlled at pH 5.5. Fermentation at pH 7.5 yielded 25600 AU/ml after 6 h, but the activity levels decreased to approximately 1000 AU/ml during the next 6 h. Adjustment of the culture pH from 6.5 to 5.5 after 6 h of fermentation extended bacST4SA activity (51200 AU/ml) over 8 h. Activity then decreased to 25600 AU/ml and was maintained this level for 10 h. Optimal levels of bacST4SA production (102400 AU/ml) were obtained after 6 h of fermentation in CSL-YE supplemented with 7.5 g/l glucose at the start of the fermentation. This level of production was maintained by changing the culture pH from 6.5 after 6 h of fermentation to pH 5.5. This study proved that bacST4SA could be produced at high levels in an inexpensive industrial medium byE. mundtii ST4SA.     

Batch and continuous cultures of<Emphasis Type="Italic"> Mannheimia succiniciproducens</Emphasis> MBEL55E for the production of succinic acid from whey and corn steep liquor

Mannheimia succiniciproducens MBEL55E isolated from bovine rumen is able to produce a large amount of succinic acid in a medium containing glucose, peptone, and yeast extract. In order to reduce the cost of the medium, whey and corn steep liquor (CSL) were used as substrates for the production of succinic acid by M. succiniciproducens MBEL55E. Anaerobic batch cultures of M. succiniciproducens MBEL55E in a whey-based medium containing CSL resulted in the production of succinic acid with a yield of 71% and productivity of 1.18 g/l/h, which are similar to those obtained in a whey-based medium containing yeast extract (72% and 1.21 g/l/h). Anaerobic continuous culture of M. succiniciproducens MBEL55E in a whey-based medium containing CSL resulted in a succinic acid yield of 69% and a succinic acid productivity as high as 3.90 g/l/h. These results show that succinic acid can be produced efficiently and economically by M. succiniciproducens MBEL55E from whey and CSL.     

Production of glucose–fructose oxidoreductase and ethanol by Zymomonas mobilis ATCC 29191 in medium containing corn steep liquor as a source of vitamins

Different concentrations of corn steep liquor (CSL) were tested in the cultivation of Zymomonas mobilis. Cell growth, ethanol production, and the formation of glucose-fructose oxidoreductase (GFOR) and glucono-delta-lactonase (GL), the enzymes responsible for the bio-production of gluconic acid and sorbitol, were examined. The cell yields using 25 g CSL l(-1) and 40 g CSL l(-1) (Y(X,S) approximately 0.031 g g(-1)) were close to that obtained with 5 g yeast extract (YE) l(-1). With 5 g CSL l(-1) and 15 g CSL l(-1), the nutritional limitation led to smaller Y(X/S). Using 100 g CSL l(-1) produced an inhibitory effect on cell growth. Similar ethanol yields (92-95%) were calculated for each concentration of CSL and also for YE medium. The highest specific GFOR/GL activities (13.2-13.5 U g(-1) dry cell) were reached with 25 g CSL l(-1) and 40 g CSL l(-1), values comparable to that achieved with 5 g YE l(-1). The results confirm that CSL is an effective and cheap supplement for Z. mobilis medium, increasing the economic potential of a large-scale bio-production of sorbitol and gluconic acid by untreated Z. mobilis cells. The economic feasibility of the process is discussed.     

Hyperproduction of N-acetylneuraminate lyase by the gene-cloned strain ofEscherichia coli

Summary Optimal culture medium for production ofN-acetylneuraminate lyase (NANA lyase) by the gene-cloned strain ofEscherichia coli, E. coli(pNALl), was screened to develop the process for the industrial production of NANA lyase. Out of nutrients tested, corn steep liquor (CSL) and sugarcane molasses were superior nutrient sources for the enzyme production. Hyperproduction (6–8 units/ml-broth) was achieved on the medium consisted of CSL and molasses.     

青霉PT95菌固态发酵产生类胡萝卜素的研究

本文对青霉Ｐｅｎｉｃｉｌｌｉｕｍｓｐ．ＰＴ９５菌株在固态发酵条件下菌核内产生类胡萝卜素进行了初步研究。结果表明,在３种固态发酵培养基中,玉米粉培养基（ＳＭＡ）比麸皮２基和棉籽壳培养基更适合于ＰＴ９５菌株固态发酵产生类胡萝卜素。为了增加菌核干重和提高类胡萝卜素产率,ＳＭＡ中需要添加氮源、碳源和植物油。在所度的各种氮、碳源中,以硝酸钠和麦芽糖效果最佳。通过我试验确定了在培养基盐溶液中添加硝酸钠３ｇ／Ｌ     

Biomass and carotenoid pigment production by patagonian native yeasts

Summary New yeast isolates from unexplored Patagonian habitats were studied for the production of biomass and carotenoids as the first step towards the selection of hyper-producing strains and the design of a process optimization approach. Patagonian yeast isolates considered as potential biomass and carotenoid sources were studied using ammonium sulphate and urea as nitrogen sources in semi-synthetic medium (MMS), and agro-industrial byproducts (cane molasses, corn syrup, raw malt extract) as carbon sources. Maximum pigment production (300 μg g⁻¹) was achieved by Rhodotorula mucilaginosa CRUB 0195 and by novel species Cryptococcus sp. CRUB 1046. β-carotene, torulene and torularhodin were the major carotenoids found.     

Valorisation of chicken feathers for xanthan gum production using Xanthomonas campestris MO-03

Xanthan gum is an important commercial polysaccharide produced by Xanthomonas species. In this study, xanthan production was investigated using a local isolate of Xanthomonas campestris MO-03 in medium containing various concentrations of chicken feather peptone (CFP) as an enhancer substrate. CFP was produced with a chemical process and its chemical composition was determined. The addition of CFP (1–8?g/l) increased the conversion of sugar to xanthan gum in comparison with the control medium, which did not contain additional supplements. The highest xanthan production (24.45?g/l) was found at the 6?g/l CFP containing control medium in 54?h. This value was 1.73 fold higher than that of control medium (14.12?g/l). Moreover, addition of CFP improved the composition of xanthan gum; the pyruvate content of xanthan was 3.86% (w/w), higher than that of the control (2.2%, w/w). The xanthan gum yield was also influenced by the type of organic nitrogen sources. As a conclusion, CFP was found to be a suitable substrate for xanthan gum production.     

Strain development and medium optimization for fumaric acid production

Rhizopus oryzae RUR709 mutant was isolated based on halo size from selection medium via mutagenesis with UV and γ-rays, and the production of fumaric acid in the submerged fermentation was assessed. The maximum concentration of fumaric acid was obtained using 0.5% corn steep liquor (CSL) as the nitrogen source. Organic nitrogen sources were shown to be more effective in fumaric acid production than inorganic nitrogen sources. Using optimum medium obtained by response surface methodology (RSM), the maximum concentration of fumaric acid achieved in flask culture was 26.2 g/L, which is fairly close to the 27.4 g/L predicted by the model. The highest concentration of fumaric acid in the stirred-tank reactor generated by the R. oryzae RUR709 mutant was 32.1 g/L and yield (0.45 g/g) and productivity (0.32 g/L/h) were highest at 4 days.     

Production of a novel polygalacturonic acid bioflocculant REA-11 by Corynebacterium glutamicum

The production of a novel polygalacturonic acid bioflocculant REA-11 from a newly isolated strain, Corynebacterium glutamicum CCTCC M201005, was investigated. Sucrose was chosen as a carbon source for REA-11 production. Complex nitrogen sources containing urea and an organic nitrogen compound enhanced both bacterial growth and REA-11 production, among which urea plus corn steep liquor was shown to be the most efficient combination. A cost-effective medium for REA-11 production mainly comprised 17 g/l sucrose, 0.45 g/l urea, and 5 ml/l corn steep liquor, under which conditions the flocculating activity reached 390 U/ml. The molar ratio of carbon to nitrogen (C/N) significantly affected REA-11 production, where a C/N ratio of 20:1 was shown to be the best. Interestingly, by simultaneously feeding sucrose and urea at a C/N ratio of 20:1 at 24 h of fermentation, REA-11 production (458 U/ml) was enhanced by 17% compared to the control. In a 10 l jar fermentor, lower dissolved oxygen tension was favorable for REA-11 production: a flocculating activity of 520 U/ml was achieved at a kappaLa of 100 h(-1). REA-11 raw product is relatively thermo-stable at acidic pH ranges of 3.0-6.5. Preliminary application studies showed that REA-11 had stronger flocculating activity to Kaolin clay suspension compared to chemical flocculants. In addition, the capability of decolorizing molasses wastewater indicates the industrial potential of this novel bioflocculant.     

Cellulose degradation and glucose accumulation byClostridium thermocellum ATCC 27405 under different cultural conditions

Effect of various cultural parameters on cellulose degradation, glucose accumulation and ethanol production byClostridium thermocellum ATCC 27405 were investigated. Optimum pH values for glucose accumulation and ethanol production were determined as 7 and 10, respectively. Highest amount of ethanol (0.92 g/l) was obtained from the culture which contains 10 g urea/l with 34.5% decrease in glucose accumulation. Addition of 100 mM phosphate to the medium increased ethanol production while cellulose degradation and sugar accumulation decreased by 34 and 99%, respectively. Among minerals tested, Mg⁺² was found to be the most important element which affects cellulose degradation. When the medium contained no Mg⁺², residual cellulose concentration was 4.3 g cellulose/l. When the cultural parameters were optimised, glucose accumulation started at early days of fermentation and glucose concentration was 60% higher than that of the control at the 10^th day of fermentation.