• Title/Summary/Keyword: Fed-batch

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Effects of Nitrogen and Oxygen Supply on Production of $Poly-{\beta}-Hydroxybutyrate$ in Azotobacter chroococcum

  • Lee, In-Young;Stegantseva, Ellen-M.;Savenkova, Ludmila;Park, Young-Hoon
    • Journal of Microbiology and Biotechnology
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    • v.5 no.2
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    • pp.100-104
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    • 1995
  • Production of $poly-{\beta}-hydroxybutyrate$ (PHB) in a strain of Azotobacter chroococcum, a nitrogen-fixing bacteria, was investigated at various levels of nitrogen and oxygen. Feeding nitrogen source increased both cell growth and PHB accumulation. Oxygen supply appeared to be one of the most important operating parameters for PHB production. Both cell growth and PHB accumulation increased with the sufficient supply of air in the fed-batch fermentation of the strain. However, it was also noted that keeping the oxygen level under limited condition was critical to achieve high PHB productivity. A high titer of PHB (52 g/l) with a high cellular content (60%) was obtained after 48 hr of fed-batch operation by controlling the oxygen supply. Dual limitation of nitrogen and oxygen did not further increase the PHB accumulation probably due to the greater demand for reducing power and ATP for nitrogen fixation.

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Enhanced Production of Antifungal Substance(PAFS) Bioxynthesized by Pseudomonas aeruginosa and Examination of Its Physiological Characteristics in Fermentation (Pseudomonas aeruginosa에 의핸 생합성되는 향진균성물질(PAFS)의 생산성 증가 및 생산균주의 배양생리학적 특성 연구)

  • 박선옥;송성기;윤권상;정연호;이상종;정용섭;전계택
    • Microbiology and Biotechnology Letters
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    • v.28 no.6
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    • pp.341-348
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    • 2000
  • Selection of high producer strain, optimization of production medium and cultivation in bioreactor system were carried out in order to produce an antifungal substance, PAFS in large amounts which sources and 41 kinds of nitrogen sources, a synthetic medium consisting of fructose(70 g/1) and ammonium sulfate (10g/l) and a complex medium including galactose(30g/l), fructose(20g/l) and cottonseed flour(35g/l) were determined as opti-mized media for PAFS production. In bioreactor studies examining physiological characteristics of the pro- ducer microorganism with the complex medium, typical pattern of diauxic growth was observed as demonstrated by the result that fructose was not used before almost exhaustion on readily utilizable carbon source, galactose. When galactose was supplemented additionally during the fermentation period. PAFS pro-ductivity did no increases any more, indicating that large portion of the added galactose was used for cell growth instead of biosynthesis of the secondary metabolite. It was deduced that PAFS production could be enhananced by employing fed-batch operation in order to overcome the apparent phenomenon of catabolite repression and /or inhibition.

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Downstream Processing of Recombinant Hirudin Produced in Saccharomyces cerevisiae

  • Chung, Bong-Hyun;Kim, Won-Kyung;Rao, K.Jagannadha;Kim, Chul-Ho;Rhee, Sang-Ki
    • Journal of Microbiology and Biotechnology
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    • v.9 no.2
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    • pp.179-183
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    • 1999
  • A recombinant form of hirudin, a potent thrombin-specific inhibitor derived from the bloodsucking leech, was expressed as a secretory product in Saccharomyces cerevisiae under the control of GALl0 promoter and the mating factor $\alpha$pre-pro leader sequence. In an attempt to produce recombinant hirudin (r-Hir) of therapeutic purity in large quantities, the fed-batch fermentation was carried out by using this recombinant yeast, and subsequently downstream processing was developed with the preparative-scale column chromatography systems. About 234 mg/l of biologically active r-Hir was produced as a secretory product by the fed-batch fermentation strategy developed for an efficient downstream processing. Using a two-step chromatography process (an anion exchange chromatography followed by the reverse phase HPLC), the r-Hir was purified to>98% with an overall recovery yield of 84%. According to the N-terminal amino acid sequencing, the purified r-Hir was found to have the predicted N-terminal amino acid sequence. The biological activity of the purified r-Hir to inhibit thrombin was also identical to that of the commercial hirudin.

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Novel Cationic Microbial Polyglucosamine Biopolymer from New Enterobacter sp. BL-2 and Its Bioflocculation Efficacy

  • SON MI-KYUNG;SHIN HYUN-DONG;HUH TAE-LIN;JANG JIN-HO;LEE YONG-HYUN
    • Journal of Microbiology and Biotechnology
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    • v.15 no.3
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    • pp.626-632
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    • 2005
  • A new bacterium BL-2 excreting a novel cationic polyglucosamine biopolymer was isolated from the spoiled leaves of Chinese cabbage and identified as Enterobacter sp. BL-2. The isolated Enterobacter sp. BL-2 was cultivated in pH-stat fed-batch culture using acetic acid as the feeding stock at pH 8.0, resulting in 17.11 g/l of cells and 1.53 g/l of an extracellular biopolymer after 72 h. The excreted biopolymer was purified by a three-step procedure, involving ethanol precipitation and deproteinizations, to a nearly homogeneous state, and its molecular weight was found to be 106 kDa. It was composed of glucosamine, rhamnose, and galactose at a molar ratio of 86.4:1.6:1.0, respectively, indicating a rarely found novel high-glucosamine-containing biopolymer. The FT-IR and $^{13}C-NMR$ spectra of the novel cationic polyglucosamine biopolymer PGB-l revealed a close identity with chitosan from crab shell. It can effectively flocculate various suspended solids, including kaolin clay, $Ca(OH)_2,\;Al_{2}O_3$, active carbon, microbial cells, and acidic dyes.

Effects of sludge and $CO_2$ addition on advanced treatment of swine wastewater by using microalgae (미세조류를 이용한 양돈폐수 고도처리에서 슬러지 및 이산화탄소의 첨가의 영향)

  • Lim, Byung-Ran;Park, Ki-Young;Lee, Ki-Say;Lee, Soo-Koo
    • Journal of Korean Society of Water and Wastewater
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    • v.25 no.3
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    • pp.307-312
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    • 2011
  • The potential of algal-bacterial culture was investigated for advanced treatment of animal wastewater. Fed-batch experiments were carried out to examine treatability of nitrogen and phosphorus in different microbial consortium: Chlorella vulgaris, activated sludge, three microalgae strains (Scenedesmus, Microcystis, Chlorella) and Bacillus consortium, and three microalgae strains and sludge consortium. Single culture of C. vugaris showed the better efficiency for nitrogen removal but was not good at organic matter and phosphorus removal compared with activated sludge. Three microalgae and Bacillus consortium was best culture among the culture and consortium for pollutants removal tested in this experiment. Effect of $CO_2$ addition was studied by using three microalgae and Bacillus consortium. $CO_2$ addition enhanced T-P removal efficiency up to 60%. However, removal efficiencies of T-N and ammonia nitrogen reduced on the contrary.

Extracellular Overproduction of $\beta$-Cyclodextrin Glucanotransferase in a Recombinant E. coli Using Secretive Expression System

  • Lee, Kwang-Woo;Shin, Hyun-Dong;Lee, Yong-Hyun
    • Journal of Microbiology and Biotechnology
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    • v.12 no.5
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    • pp.753-759
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    • 2002
  • $\beta$-Cyclodextrin glucanotransferase ($\beta$-CGTase) was overproduced extracellularly using recombinant E. coli by transforming the plasmid pECGT harboring a secretive signal peptide. The $\beta$-CGTase gene of alkalophilic Bacillus firmus var alkalophilus was inserted into the high expression vector pET20b(+) containing a secretive pelB signal peptide, and then transformed into E. coli BL2l(DE3)pLysS. The optimum culture conditions fer the overproduction of $\beta$-CGTase were determined to be TB medium containing 0.5% (w/v) soluble starch at post-induction temperature of $25^{\circ}C$. A significant amount of $\beta$-CGTase, up to 5.83 U/ml, which was nine times higher than that in the parent strain B. firmus var. alkalophilus, was overproduced in the extracellular compartment. A pH-stat fed-batch cultivation of the recombinant E. coli was also performed to achieve the secretive overproduction of $\beta$-CGTase at a high cell density, resulting in production of up to 21.6 U/ml of $\beta$-CGTase.

Novel SSF Process for Ethanol Production from Microcrystalline Cellulose Using the $\delta$-Integrated Recombinant Yeast, Saccharomyces cerevisiae L2612$\delta$GC

  • Cho, Kwang-Myung;Yoo, Young-Je
    • Journal of Microbiology and Biotechnology
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    • v.9 no.3
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    • pp.340-345
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    • 1999
  • A novel simultaneous saccharification and fermentation (SSF) process from the microcrystalline cellulose to ethanol was developed by using $\delta$-integrated recombinant cellulolytic Saccharomyces cerevisiae L2612$L2612\deltaGC$, which can utilize cellulose as carbon and energy sources. The optimum amount of enzymes needed for the efficient conversion of cellulose to ethanol at $30^{\circ}C$ was determined with commercial cellulolytic enzymes. By fed-batch cultivation, the heterologous cellulolytic enzymes were accumulated up to 42.67% of the total cellulase and 29% of the $\beta$-glucosidase needed for the efficient SSF process. When this $\delta$-integrated recombinant yeast was applied to the successive SSF step for ethanol production, 20.35 g/l of ethanol was produced after 12 h from 50 g/l of microcrystalline cellulose. By using this novel SSF process, a considerable amount of commercial enzymes was reduced.

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Optimum Conditions for the Production of Tetramethylpyrazine Flavor Compound by Aerobic Fed-batch Culture of Lactococcus lactis subsp. lactis biovar. diacetylactis FC1

  • HYONG-JOO LEE;KIM, KWANG-SOO;DONG-HWA SHON;DAE-KYUN CHUNG
    • Journal of Microbiology and Biotechnology
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    • v.4 no.4
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    • pp.327-332
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    • 1994
  • Optimum conditions for the production of acetoin and ammonia as the precursors of tetramethylpyrazine(TMP) were determined using Lactococcus lactis subsp. lactis biovar. diacetylactis FC1 in a modified Lactose-citrate broth containing galactose, citrate, and arginine. The cell growth and the productivity of acetoin and ammonia were remarkably increased in an aerobic culture with 10 $\mu M$ of hematin. For the optimum conditions of acetoin and ammonia production, the concentration of citrate and arginine were adjusted to 156 mM and 50 mM after 18 hr cultivation, and citrate and galactose to 156 mM and 50 mM after 36 hr cultivation, respectively. In these conditions, acetoin and ammonia were produced to the final concentration of 127 mM and 195 mM, which were the highest concentations, respectively. The optimum conditions of the TMP production were also determined as follows; 4 hours at 121, pH 8.3, and the maximal yield of TMP under these conditions was 0.81 g/l.

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Production of Poly($\beta$-hydroxybutyrate-co-$\beta$-hydroxyvalerate) by Two-stage Fed-batch Fermentation of Alcaligenes eutrophus

  • Lee, In-Young;Kim, Guk-Jin;Shin, Yong-Cheol;Chang, Ho-Nam;Park, Young-Hoon
    • Journal of Microbiology and Biotechnology
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    • v.5 no.5
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    • pp.292-296
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    • 1995
  • Production of poly($\beta$-hydroxybutyrate-co-$\beta$-hydroxyvalerate)[poly(HB-co-HV) from glucose and propionic acid was studied in a two-stage fed-batch fermentation using Alcaligenes eutrophus NCIMB 11599. When either glucose became sufficient or the feeding rate of propionic acid decreased, production of poly(HB-co-HV) increased but concomitantly resulted in a reduced fraction of HV. During the copolymer accumulation stage, the specific production rate of hydroxyvalerate (HV) increased up to 0.013 (g-HV/g-RCM/h) but it decreased as propionic acid was accumulated. Control of the propionic acid concentration in the medium, therefore, is considered to be one of the most important operating parameters for production of poly(HB-co-HV) with a higher HV fraction. A high titre of poly(HB-co-HV) (85.6 g/I) with HV fraction of 11.4 mol$%$ could be obtained in 50 h by controlling the propionic acid concentration at 1 to 4 g/I.

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Mcl-PHAs Produced by Pseudomonas sp. Gl01 Using Fed-Batch Cultivation with Waste Rapeseed Oil as Carbon Source

  • Mozejko, Justyna;Wilke, Andreas;Przybylek, Grzegorz;Ciesielski, Slawomir
    • Journal of Microbiology and Biotechnology
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    • v.22 no.3
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    • pp.371-377
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    • 2012
  • The present study describes medium-chain-length polyhydroxyalkanoates (mcl-PHAs) production by the Pseudomonas Gl01 strain isolated from mixed microbial communities utilized for PHAs synthesis. A two-step fed-batch fermentation was conducted with glucose and waste rapeseed oil as the main carbon source for obtaining cell growth and mcl-PHAs accumulation, respectively. The results show that the Pseudomonas Gl01 strain is capable of growing and accumulating mcl-PHAs using a waste oily carbon source. The biomass value reached 3.0 g/l of CDW with 20% of PHAs content within 48 h of cultivation. The polymer was purified from lyophilized cells and analyzed by gas chromatography (GC). The results revealed that the monomeric composition of the obtained polyesters depended on the available substrate. When glucose was used in the growth phase, 3-hydroxyundecanoate and 3-hydroxydodecanoate were found in the polymer composition, whereas in the PHAs-accumulating stage, the Pseudomonas Gl01 strain synthesized mcl-PHAs consisting mainly of 3-hydroxyoctanoate and 3-hydroxydecanoate. The transcriptional analysis using reverse-transcription real-time PCR reaction revealed that the phaC1 gene could be transcribed simultaneously to the phaZ gene.