Changes of Curdlan Biosynthesis and Nitrogenous Compounds Utilization Characterized in <Emphasis Type="Italic">ntrC</Emphasis> Mutant of <Emphasis Type="Italic">Agrobacterium</Emphasis> sp. ATCC 31749

The regulatory function of global regulator NtrC on curdlan biosynthesis and nitrogen consumption under nitrogen-limited condition in Agrobacterium sp. ATCC 31749 was investigated. The ntrC mutant of Agrobacterium sp. was constructed by homologous recombination. The ability to utilize NH₄Cl and KNO₃ was impaired in the mutant. Other nitrogenous compounds, such as glutamic acid and glutamine, were utilized normally. Curdlan production capability was impaired severely in the mutant. Curdlan production was 5-fold lower than the wild type strain in batch fermentation with NH₄Cl as the sole nitrogen source. However, up to 6.5 g l⁻¹ of a newly found alkali-insoluble biopolymer was produced by the ntrC mutant when glutamic acid was used as nitrogen source. The new biopolymer had glycosidic bond and hydroxyl group but no β-configuration absorption peak on IR spectrum was found as different from curdlan. In addition, the mutant exhibited a rapid morphological change from the dot to rod form. These results deduced that the global regulator NtrC was involved in curdlan and other biopolymer biosynthesis in Agrobacterium sp. ATCC 31749 in response to nitrogen-limited condition.     

Improved curdlan fermentation process based on optimization of dissolved oxygen combined with pH control and metabolic characterization of <Emphasis Type="Italic">Agrobacterium</Emphasis> sp. ATCC 31749

A significant problem in scale-down cultures, rarely studied for metabolic characterization and curdlan-producing Agrobacterium sp. ATCC 31749, is the presence of dissolved oxygen (DO) gradients combined with pH control. Constant DO, between 5% and 75%, was maintained during batch fermentations by manipulating the agitation with PID system. Fermentation, metabolic and kinetic characterization studies were conducted in a scale-down system. The curdlan yield, intracellular nucleotide levels and glucose conversion efficiency into curdlan were significantly affected by DO concentrations. The optimum DO concentrations for curdlan production were 45–60%. The average curdlan yield, curdlan productivity and glucose conversion efficiency into curdlan were enhanced by 80%, 66% and 32%, respectively, compared to that at 15% DO. No apparent difference in the gel strength of the resulting curdlan was detected. The comparison of curdlan biosynthesis and cellular nucleotide levels showed that curdlan production had positive relationship with intracellular levels of UTP, ADP, AMP, NAD⁺, NADH and UDP-glucose. The curdlan productivity under 45% DO and 60% DO was different during 20–50 h. However, after 60 h curdlan productivity of both conditions was similar. On that basis, a simple and reproducible two-stage DO control process for curdlan production was developed. Curdlan production yield reached 42.8 g/l, an increase of 30% compared to that of the single agitation speed control 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.     

Biotransformation of Panax notoginseng saponins into ginsenoside compound K production by Paecilomyces bainier sp. 229

Aims: Development and optimization of an efficient and inexpensive biotransformation process for ginsenoside compound K production by Paecilomyces bainier sp. 229. Methods and Results: We have determined the optimum culture conditions required for the efficient production of ginsenoside compound K by P. bainier sp. 229 via biotransformation of ginseng saponin substrate. The optimal medium constituents were determined to be: 30 g sucrose, 30 g soybean steep powder, 1 g wheat bran powder, 1 g (NH₄)₂SO₄, 2 g MgSO₄·7H₂O and 1 g CaCl₂ in 1 l of distilled water. An inoculum size of 5–7·5% with an optimal pH range of 4·5–5·5 was essential for high yield. Conclusions: The Mol conversion quotient of ginseng saponins increased from 21·2% to 72·7% by optimization of the cultural conditions. Scale‐up in a 10 l fermentor, under conditions of controlled pH and continuous air supply in the optimal medium, resulted in an 82·6% yield of ginsenoside compound K. Significant and Impact of the Study: This is the first report on the optimization of culture conditions for the production of ginsenoside compound K by fungal biotransformation. The degree of conversion is significantly higher than previous reports. Our method describes an inexpensive, rapid and efficient biotransformation system for the production of ginsenoside compound K.     

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.     

Optimizing emulsan production of <Emphasis Type="Italic">A. venetianus</Emphasis> RAG-1 using response surface methodology

Statistical experimental design was used to optimize medium constituents for emulsan production by Acinetobacter venetianus RAG-1 in batch cultivation. The factors affecting emulsan production were screened by a two-level factorial design, and the optimal concentration of medium constituents for emulsan production were determined by the method of steepest path ascent and central composite experimental design. Experimental results showed that the optimal medium constituents were 9.16 g/L ethanol, 8.2 g/L KH₂PO₄, 23.32 g/L K₂HPO₄, 5.77 g/L (NH₄)₂SO₄ and 0.354 g/L MgSO₄•7H₂O. Under this optimal composition, the predicted emulsan production was 72.198 mg/L, and experimental value was 73.312 mg/L for 80 h culture in the shake flasks, and the emulsan yield by A. venetianus RAG-1 was enhanced nearly 1.48-fold (from 49.5 to 73.312 mg/L). Based on the results, we identify the optimal medium constituents for emulsan production and could take advantage of strategy for scale up the fermentation of emulsan production.     

Isolation,screening, and selection of an L-glutaminase producer from soil and media optimization using a statistical approach

A culture isolated from garden soil was found to be a promising L-glutaminase producer. Biochemical identification tests and 16S rRNA sequencing identified this isolate to be Klebsiella oxytoca. Subsequently, media optimization using one-factor-at-a-time approach and response surface methodology was undertaken. A face centered central composite design was employed to investigate the interactive effects of four variables, viz. concentrations of maltose, yeast extract, beef extract, and ammonium acetate on glutaminase production. Almost all factors had significant interactive effects on glutaminase production. A medium containing (g/L): maltose, 23.31; yeast extract, 20.0; beef extract, 20.01; ammonium acetate, 10.0; mannitol, 10.0; KH₂PO₄, 0.4; Na₂SO₄, 0.4; and MgCl₂, 0.4 was optimum for glutaminase production. The applied methodology was validated using this optimized media and enzyme activity of 458.91 ± 9.49 U/L and specific activity of 0.441 ± 0.04 U/mg protein after 42 h of incubation at 33°C were obtained.     

Recent advances in curdlan biosynthesis,biotechnological production,and applications

Curdlan is a water-insoluble β-(1,3)-glucan produced by Agrobacterium species under nitrogen-limited condition. Its heat-induced gelling properties render curdlan to be very useful in the food industry initially. Recent advances in the understanding of the role curdlan plays in both innate and adaptive immunity lead to its growing applications in biomedicine. Our review focuses on the recent advances on curdlan biosynthesis and the improvements of curdlan fermentation production both from our laboratory and many others as well as the latest advances on the new applications of curdlan and its derivatives particularly in their immunological functions in biomedicine.     

An increase of curdlan productivity by integration of carbon/nitrogen sources control and sequencing dual fed-batch fermentors operation

Curdlan is produced by Agrobacterium sp. ATCC 31749 under nitrogen-limited conditions not associated with cell growth. A novel curdlan production process was developed based on the different nutrient requirements for microbial cell growth and its efficiency was increased by integrating carbon/nitrogen sources control and sequencing dual fed-batch fermentors operation. By feeding ammonium solution to supply abundant nitrogen source and controlling pH in Fermentor I, cell growth was accelerated. High cell density of 29 g/L was attained. The culture broth in Fermentor I was then inoculated into sequencing Fermentor II which alleviated the high requirement for dissolved oxygen and accumulation of inhibitory metabolic by-products during curdlan production. Fermentor I promoted cell growth. Curdlan production started instantaneously in Fermentor II. By feeding nutrient solution with high carbon/nitrogen ratio and NaOH solution for pH adjustment, a feasible and optimal curdlan production process was formulated. The productivity, conversion efficiency and curdlan yield were achieved of 0.98 g/(L h), 57% (w) and 67 g/L, respectively. Such novel process can be scaled up for significant cost reduction at the industrial level.     

Effect of pretreatment chemicals on xylose fermentation by Pichia stipitis

Pretreatment of biomass with dilute H₂SO₄ results in residual acid which is neutralized with alkalis such as Ca(OH)₂, NaOH and NH₄OH. The salt produced after neutralization has an effect on the fermentation of Pichia stipitis. Synthetic media of xylose (60 g total sugar/l) was fermented to ethanol in the presence and absence of the salts using P. stipitis CBS 6054. CaSO₄ enhanced growth and xylitol production, but produced the lowest ethanol concentration and yield after 140 h. Na₂SO₄ inhibited xylitol production, slightly enhanced growth towards the end of fermentation but had no significant effect on xylose consumption and ethanol concentration. (NH₄)₂SO₄ inhibited growth, had no effect on xylitol production, and enhanced xylose consumption and ethanol production.     

一株产褐藻胶裂解酶的需钠弧菌筛选及酶解产物分析

[背景]褐藻胶裂解酶种类丰富、降解机制多样,是高效环保降解褐藻胶、制备褐藻寡糖的工具酶,成为褐藻植物高值化开发利用的研究热点.[目的]从海泥中筛选获得褐藻胶裂解酶高效产酶菌株,确定菌株发酵产酶最优条件,鉴定和分析酶降解产物,进而解析该酶的降解特性.[方法]以褐藻胶为唯一碳源,从海带养殖场附近海泥中筛选菌株,通过形态学观...     

Effect of nitrogen source on the antimicrobial activity of the bacilli air flora

The antimicrobial activity of strainsBacillus megaterium NB-3,Bacillus cereus NB-4,Bacillus cereus NB-5,Bacillus subtilis NB-6 andBacillus circulans NB-7, previously isolated from the air flora, now in the Jerash Culture Collection (Jordan), was investigated in media containing different nitrogen sources. Maximum antimicrobial activity of strains NB-4, NB-5 and NB-6 was observed using Ca(NO₃)₂ as nitrogen source, (NH₄)₂SO₄ and KNO₂ strongly enhanced the antimicrobial activity of strains NB-3 and NB-7, respectively. The lowest level of the antimicrobial activity of strains NB-4 and NB-5 was observed using NaNO₃. In case of strains NB-3, NB-6 and NB-7, the lowest antimicrobial activity was observed using NH₄NO₃, KNO₃ and (NH₄)₂SO₄ as nitrogen source, respectively.     

Optimization of fermentation conditions for production of anti-TMV extracellular ribonuclease by Bacillus cereus using response surface methodology

Bacillus cereus ZH14 was previously found to produce a new type of antiviral ribonuclease, which was secreted into medium and active against tobacco mosaic virus. In order to enhance the ribonuclease production, in this study the optimization of culture conditions using response surface methodology was done. The fermentation variables including culture temperature, initial pH, inoculum size, sucrose, yeast extract, MgSO₄·7H₂O, and KNO₃ were considered for selection of significant ones by using the Plackett–Burman design, and four significant variables (sucrose, yeast extract, MgSO₄·7H₂O, and KNO₃) were further optimized by a 2⁴ factorial central composite design. The optimal combination of the medium constituents for maximum ribonuclease production was determined as 8.50 g/l sucrose, 9.30 g/l yeast extract, 2.00 g/l MgSO₄·7H₂O, and 0.62 g/l KNO₃. The enzyme activity was increased by 60%. This study will be helpful to the future commercial development of the new bacteria-based antiviral ribonuclease fermentation process.     

钾肥类型对菜心(菜薹)生长、细胞保护酶和内源激素的影响

为探讨钾肥类型对菜心(Brassica campestris L. ssp. chinensis var. utilis Tsen et Lee)的作用效应,研究了不同钾肥类型和水平对菜心生长、细胞保护酶和内源激素的影响。结果表明,氯化钾或硫酸钾处理可提高菜心叶片的POD 和CAT 活性、IAA 和GA₃ 含量,降低MDA 含量,提高菜薹产量。随着钾水平的提高,叶片IAA 和GA₃ 含量、POD 和CAT 活性以及菜薹质量明显提高,MDA 含量降低。当施钾90 kg hm^-2 时,叶片的GA₃ 和IAA 含量显著下降,而POD 活性和菜薹产量没有显著变化。在相同水平下,氯化钾与硫酸钾对植株生长、菜薹产量、叶片GA₃ 含量的影响不显著。当施钾0~90 kg hm^-2 时,氯化钾处理的叶片POD 活性显著高于硫酸钾处理;而施钾135~180 kg hm^-2 时,氯化钾处理的叶片POD 活性则显著低于硫酸钾处理。除了90 kg hm^-2 氯化钾处理的CAT 活性和45 kg hm^-2 氯化钾处理的MDA 含量低于硫酸钾处理以及90 kg hm^-2 和180 kg hm^-2 氯化钾处理的IAA 含量高于硫酸钾处理的外,相同水平氯化钾和硫酸钾处理的CAT 活性、MDA 含量和IAA 含量没有显著差异。可见,钾肥类型对菜心的活性氧代谢系统及内源激素含量有一定的影响,但氯化钾与硫酸钾对菜心的施用效果相当,生产上可采用氯化钾代替硫酸钾以节约肥料成本,K₂O 施用量以90 kg hm^-2 为宜。     

Application of statistically-based experimental designs in medium optimization for spore production of <Emphasis Type="Italic">Bacillus subtilis</Emphasis> from distillery effluent

Spore production of Bacillus subtilis from distillery effluent was optimized using statistically-based experimental designs. The two-level Plackett–Burman design was applied to choose the nutrient supplements significantly influencing spore production. Among the seven variables we tested, the most significant variables influencing spore production were statistically elucidated for optimization, and included (NH₄)₂SO₄, corn flour and MgSO₄. The optimum concentration of each significant variable was then predicted using Box–Behnken design. A second-order polynomial was determined by the multiple regression analysis of this experimental data. The optimum values for the critical nutrient supplements for the maximum were obtained as followed: (NH₄)₂SO₄, 4.54%; corn flour, 1.2%; MgSO₄, 0.56% with the corresponding value of maximum spore production of 7.24 × 10⁸ spores/ml. A verification experiment performed under the optimum conditions resulted in 6.95 × 10⁸ spores/ml. The determination coefficient (R ²) was 0.98, which ensure an adequate credibility of the model.     

Effect of H2SO4, HCl and Al2(SO4)3 on the yield,chemical composition and Ca uptake from applied Ca45CO3 by dhaincha (Sesbania aculeata Pers.) in a saline alkali soil

Summary Application of CaCO₃ and a lime-solubilizing agent (viz H₂SO₄, HCl, and Al₂(SO₄)₃) to a saline-alkali soil caused a significant increase in the dry matter yield of dhaincha (Sesbania aculeata Pers). The extent of yield enhancement by these amendments was in the decreasing order: HCl, H₂SO₄ and Al₂(SO₄)₃. Calcium content in the plant increased significantly with the application of these amendments and it was in the decreasing order: H₂SO₄, Al₂(SO₄)₃ and HCl. The uptake of Ca from native CaCO₃ was much less than that from the added Ca⁴⁵CO₃. Phosphorus content in the plant increased with the HCl and H₂SO₄ treatments and decreased with the Al₂(SO₄)₃ treatments. Nitrogen and Na contents decreased with the addition of these amendments. re]19730521     

Production of Alcaligenes xylosoxydans EMS33 in a Bench-scale Fermenter

Summary Optimization of medium composition and pH for chitinase production by the Alcaligenes xylosoxydans mutant EMS33 was carried out in the present study and the optimized medium composition and conditions were evaluated in a fermenter. The medium components screened initially using Plackett–Burman design were (NH₄)₂SO₄, MgSO₄ 7H₂O, KH₂PO₄, yeast extract, Tween 20 and chitin in shake flask experiments. The significant medium components identified by the Plackett–Burman method were MgSO₄ 7H₂O, Tween 20 and chitin. Central composite response surface methodology was applied to further optimize chitinase production. The optimized values of MgSO₄ 7H₂O, Tween 20, chitin and pH were found to be 0.6 g/l, 0.05 g/l, 11.5 g/l and 8.0, respectively. Chitinase and biomass production of Alcaligenes xylosoxydans EMS33, was studied in a 2-l fermenter containing (g/l): chitin, 11.5; yeast extract, 0.5; (NH₄)₂SO₄, 1; MgSO₄ 7H₂O, 0.6; KH₂PO₄, 1.36 and Tween 20, 0.05. The highest chitinase production was 54 units/ml at 60 h and pH 8.0 when the dissolved O₂ concentration was 60%, whereas the highest biomass production was achieved at 36 h and pH 7.5 without any dissolved O₂ control.     

Effect of nitrogen source concentration on curdlan production by Agrobacterium sp. ATCC 31749 grown on prairie cordgrass hydrolysates

The effect of nitrogen source concentration on the production of the polysaccharide curdlan by the bacterium Agrobacterium sp. ATCC 31749 from hydrolysates of prairie cordgrass was examined. The highest curdlan concentrations were produced by ATCC 31749 when grown on a medium containing a solids-only hydrolysate and the nitrogen source ammonium phosphate (2.2 mM) or on a medium containing a complete hydrolysate and 3.3 mM ammonium phosphate. The latter medium sustained a higher level of bacterial curdlan production than the former medium after 144 hr. Biomass production by ATCC 31749 was highest after 144 hr when grown on a medium containing a solids-only hydrolysate and 2.2 or 8.7 mM ammonium phosphate. On the medium containing the complete hydrolysate, biomass production by ATCC 31749 was highest after 144 hr when 3.3 mM ammonium phosphate was present. Bacterial biomass production after 144 hr was greater on the complete hydrolysate medium compared to the solids-only hydrolysate medium. Curdlan yield produced by ATCC 31749 after 144 hr from the complete hydrolysate medium containing 3.3 mM ammonium phosphate was higher than from the solids-only hydrolysate medium containing 2.2 mM ammonium phosphate.     

Bioconversion of municipal solid waste to glucose for bio-ethanol production

Selected biodegradable municipal solid waste fractions were subjected to fifteen different pre-hydrolysis treatments to obtain the highest glucose yield for bio-ethanol production. Pre-hydrolysis treatments consisted of dilute acid (H₂SO₄, HNO₃ or HCl, 1 and 4%, 180 min, 60°C), steam treatment (121 and 134°C, 15 min), microwave treatment (700 W, 2 min) or a combination of two of them. Enzymatic hydrolysis was carried out with Trichoderma reesei and Trichoderma viride (10 and 60 FPU g⁻¹ substrate). Glucose yields were compared using a factorial experimental design. The highest glucose yield (72.80%) was obtained with a pre-hydrolysis treatment consisting of H₂SO₄ at 1% concentration, followed by steam treatment at 121°C, and enzymatic hydrolysis with Trichoderma viride at 60 FPU g⁻¹ substrate. The contribution of enzyme loading and acid concentration was significantly higher (49.39 and 47.70%, respectively), than the contribution of temperature during steam treatment (0.13%) to the glucose yield.     

Response surface methodology for optimization of medium components in submerged culture of Aspergillus flavus for enhanced heparinase production

Aims: Aim of the study was to develop a medium for optimal heparinase production with a strain of Aspergillus flavus (MTCC‐8654) by using a multidimensional statistical approach. Methods and Results: Statistical optimization of intracellular heparinase production by A. flavus, a new isolate, was investigated. Plackett–Burman design was used to evaluate the affect of medium constituents on heparinase yield. The experimental results showed that the production of heparinase was dependent upon heparin, the inducer; chitin, structurally similar to heparin and NH₄NO_3, the nitrogen source. A central composite design was applied to derive a statistical model for optimizing the composition of the fermentation medium for the production of heparinase enzyme. The optimum fermentation medium consisted of (g l^?1) Mannitol, 8·0; NH₄NO₃, 2·5; K₂HPO₄, 2·5; Na₂HPO₄, 2·5; MgSO₄.7H₂O, 0·5; Chitin, 17·1; Heparin, 0·6; trace salt solution (NaMoO₄.2H₂O, CoCl₂.6H₂O, CuSO₄.5H₂O, FeSO₄.7H₂O, CaCl₂), 10^?4 mol l^?1. Conclusions: A 2·37‐fold increase in heparinase production was achieved in economic and effective manner by the application of statistical designs in medium optimization. Significance and Impact of the Study: Heparinase production was doubled by statistical optimization in a cost‐effective manner. This heparinase can find application in pharmaceutical industry and for the generation of low‐molecular‐weight heparins, active as antithrombotic and antitumour agents.