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.     

Heterotrophic cultivation of Euglena gracilis Z for efficient production of α-tocopherol

Effects of hydrodynamic stress, dissolved oxygen (DO) concentration and carbon sources on heterotrophic α-tocopherol production by Euglena gracilis were investigated. In a jar fermentor without baffle plates, increasing the agitation speed up to 500 rpm had no significant effect on cell growth and α-tocopherol production. However, in a jar fermentor equipped with baffle plates, both the cell growth and α-tocopherol production were highly suppressed at 500 rpm. At high hydrodynamic stress, the cells secreted nucleic acid-related substances to the culture broth and the shape of the cells shifted from elongated toward spherical. High DO concentration had adverse effects on both cell growth and α-tocopherol production, the optimum DO concentration being below 0.8 ppm. In comparison with glucose, the growth rate was lower but the α-tocopherol content of the cells was almost four times higher when ethanol was used as the organic carbon source. In a fed-batch culture with ethanol, a very high cell concentration of 39.5 g L^-1 was obtained with α-tocopherol content of 1200 μg g-cell^-1. This α-tocopherol content is very close to the values reported for photoautotrophic and photoheterotrophic cultures. A very high α-tocopherol productivity of 102 μg L^-1 h^-1 was obtained, indicating that heterotrophic cultivation of E. gracilis has a very high potential as a substitute for the current method of extraction from vegetable oils. This revised version was published online in June 2006 with corrections to the Cover Date.     

营养条件和流加发酵对放射型根瘤菌(Rhizobium radiobacter)产辅酶Q10的影响

利用放射型根瘤菌WSH2 6 0 1(RhizobiumradiobacterWSH2 6 0 1)重点考察了葡萄糖、蔗糖、玉米浆和蛋白胨、添加物以及流加发酵对细胞生长和产辅酶Q1 0 的影响 ,结果表明 ,葡萄糖和蔗糖适合于生产辅酶Q1 0 的最佳浓度分别为 30g L和 40g L ;辅酶Q1 0 发酵时玉米浆和蛋白胨的最适浓度分别为 11g L和 16g L ;添加蕃茄汁、玉米浆能提高发酵液的生物量 ,玉米浆、异戊醇、L 甲硫氨基酸等能促进辅酶Q1 0 的积累 ;与分批发酵相比 ,在 7L罐上流加蔗糖其细胞生物量 (DCW)和辅酶Q1 0 积累量增加 ,若在流加蔗糖的同时流加适当浓度的玉米浆能显著提高辅酶Q1 0 的产量 ,最大产量达到 5 2 .4mg L ;最大生物量 (DCW)和胞内辅酶Q1 0 含量 (C B值 )分别达到 2 6 .4g L和 2 .38mg g DCW ,比不流加的分批发酵分别提高 5 3 %和 33% ,比只流加蔗糖分别提高 2 4%和 2 6 %。     

Laccase-induced C–N coupling of substituted <Emphasis Type="Italic">p</Emphasis>-hydroquinones with <Emphasis Type="Italic">p</Emphasis>-aminobenzoic acid in comparison with known chemical routes

Magnetotactic bacteria are difficult to grow under defined conditions in culture, which has presented a major obstacle to commercial application of magnetosomes. We studied the relationships among the cell growth, magnetosome formation, dissolved oxygen concentration (DO), and the ability to supply oxygen to the cells. Mass culture of Magnetospirillum gryphiswaldense MSR-1 for the production of magnetosomes was established in a 42-L fermentor under the following conditions: (1) sterile air was the sole gas supplied in the fermentor, and DO could be regulated at any level below 10% saturation by cascading the stir rate to DO, (2) to resolve the paradoxical situation that the cell growth requires higher DO whereas magnetosome formation requires low DO below the detectable range of regular oxygen electrode, DO was controlled to optimal level using the change of cell growth rate, rather than reading from the highly sensitive oxygen electrode, as the signal for determining appropriate DO, and (3) timing and rate of supplying the substrates were determined by measuring cell density and Na-lactate concentration. Under these conditions, cell density (OD565) of strain MSR-1 reached 7.24 after 60-h culture in a 42-L fermentor, and cell yield (dry weight) was 2.17 g/L, the highest yield so far being reported. The yield of magnetosomes (dry weight) was 41.7 mg/L and 16.7 mg/L/day, which were 2.8 and 2.7 times higher than the previously reported yields.     

Production of bacterial cellulose by Acetobacter xylinum BPR2001 using molasses medium in a jar fermentor

Bacterial cellulose (BC) production by Acetobacter xylinum subsp. sucrofermentans BPR2001 using molasses medium was carried out in a jar fermentor. When molasses was subjected to H₂SO₄-heat treatment, the maximum BC concentration increased to 76% more than that achieved using untreated molasses, and the specific growth rate increased 2-fold. When the initial sugar concentrations in the H₂SO₄-heat treated molasses were varied from 23 g/l to 72 g/l, BC concentration, production rate, and yield were maximum at sugar concentrations of 23 g/l and 37 g/l, and production of by-products, such as polysaccharides and CO₂, was lower than at sugar concentrations of 48 g/l and 72 g/l, indicating that maintaining a lower molasses concentration is essential for efficient BC production in jar fermentors, this being due mainly to the complex nature of molasses. Molasses has a clear advantage over pure sugars as a carbon source from an economic viewpoint.     

以玉米浆和木薯为原料机械搅拌发酵制备细菌纤维素的研究

本文以玉米浆和木薯为原料,用机械搅拌式发酵罐制备细菌纤维素（BC）,对发酵过程的纤维素产量、还原糖消耗、溶氧变化和茵浓变化进行了监测,并以葡萄糖一蛋白胨-酵母粉培养基为对照进行了比较。实验得出玉米浆作氮源时不溶BC的产量为9．2g／L,而氮源成本只是对照组的15％;木薯水解液作碳源时的不溶BC产量达到11．7g／L,比对照组（10．8g／L）高8％;而用玉米浆搭配木薯水解液发酵生产BC,产量也达到10．1g／L,验证了这两种天然原料的廉价高效性,用于工业生产细菌纤维素具有良好的前景。     

营养及环境因素对黄色短杆菌发酵生产L-亮氨酸的影响

目的:研究葡萄糖、玉米浆、蛋氨酸等主要营养物质以及环境因素对发酵生产L-亮氨酸的影响。方法:应用单因素实验确定发酵条件,采用高效液相色谱法测定产量。结果:在最优发酵条件下,以种龄36h、接种量为10%,摇瓶产L-亮氨酸的量可达19.4g/L,采用10L罐分批补料发酵64h可积累29.47g/L的亮氨酸。结论:营养及环境因素对发酵生产L-亮氨酸具有重要影响。     

Growth Profile of Crown Gall Cells of Tobacco in Suspension Culture

In order to obtain a basic information of plant cell suspension culture as a step toward the development of large scale culture, culture conditions of crown gall cells (auxin non-requiring cells) were investigated. Addition of yeast extract to culture medium was significantly effective for the growth and cell dispersion.

In experiments on the ability of the cultured cells to utilize sugars as the carbon source, it was observed that galactose, added to the culture medium, markedly inhibited the cell growth.

Pasteurization of the medium containing fructose as carbon source made it brownish by Maillard reaction and the medium apparently restrained the cell growth. However, the fructose medium sterilized by filtration was excellent for the cell growth as well as sucrose or glucose medium. In a jar fermentor, even the glucose medium became brownish by heat sterilization and the brown colored medium restrained the cell growth. Under optimum conditions, the doubling time was 1.1 day in exponential phase and 2.0 g of cell (dry weight) per 100 ml culture was obtained as the maximum yield.     

Bacterial cellulose production by fed-batch fermentation in molasses medium

Batch and fed-batch fermentations for bacterial cellulose (BC) production using molasses as a carbon source by Acetobacter xylinum BPR2001 were carried out in a jar fermentor. For improvement of BC production, molasses was subjected to H2SO4-heat treatment. The maximum BC concentration by this treated molasses increased 76%, and the specific growth rate increased 2-fold compared with that by untreated molasses. In batch fermentation, when the initial sugar concentrations of H2SO4-heat-treated molasses were varied from 20 to 70 g/L, the highest value of maximum BC concentration of 5.3 g/L was observed at 20 g/L. BC production in intermittent fed-batch (IFB) fermentation was conducted referring to the data in batch fermentation, and the highest BC production of 7.82 g/L was obtained when 0.2 L of molasses medium was added five times. When continuous fed-batch (CFB) fermentations were conducted, maximum BC concentration was obtained with a feeding rate of 6.3 g-sugar/h, which was derived from the optimal IFB experiment.     

Bacterial cellulose production under oxygen-enriched air at different fructose concentrations in a 50-liter, internal-loop airlift reactor

Bacterial cellulose (BC) production by Acetobacter xylinum subsp. sucrofermentans BPR2001 was carried out in a 50-1 internal-loop airlift reactor in air at an initial fructose concentration of 40 g/l. The BC production rate was 0.059 g/l per h. When oxygen-enriched air was supplied instead of air, the BC production rate increased to 0.093 g/l per h, and the BC yield was enhanced from 11% in air to 18%. When the initial fructose concentrations were varied from 30 to 70 g/l, the highest BC yield (35%) the highest production rate (0.22 g/l x per h), and the highest concentration of BC produced (10.4 g/l) were observed at 60-70 g/l fructose. From the carbon mass balance calculated at the final stage of cultivation, it was observed that enhanced BC production was reflected as a decrease in both CO2 evolution and the concentration of other unknown substances, suggesting the efficient utilization of energy for BC synthesis despite O2 limitation.     

Preferential and high-yield production of a cephamycin C by dissolved oxygen controlled fermentation

Streptomyces sp. P6621-RS1726, a high cephamycin C producing mutant, usually produces cephamycin C together with its precursor, penicillin N, in flask fermentation. The fermentation conditions for selective and high yield production of cephamycin C were investigated using 20-l jar fermentors. As a result, cephamycin C was preferentially produced without penicillin N when the DO level was maintained at least higher than at 10% during the production phase. However, when the agitation speed was too high at the initial stage of the fermentation, the cell growth was inhibited, resulting in suppression of both cephamycin C and penicillin N production, even if the DO was maintained at a high level. Based on these experiments, a computer control system for preferential and high-yield production of cephamycin C was constructed. By using this computer control system, scale-up from a 20-l jar fermentor to a 1,500-l pilot fermentor was carried out with control of the DO level at 20% of saturation during the cephamycin C production phase. As a result, the profile of cephamycin C production in the former was favorably reproduced in the latter.     

Controlling substrate concentration in fed-batch candida magnoliae culture increases mannitol production

Candida magnoliae HH-01, a yeast strain that is currently used for the industrial production of mannitol, has the highest mannitol production ever reported for a mannitol-producing microorganism. However, when the fructose concentration exceeds 150 g/L, the volumetric mannitol production rate decreases because of a lag in mannitol production, and the yield decreases as a result of the formation of side products. In fed-batch culture, the volumetric production rate and mannitol yield from fructose vary substantially with the fructose concentration and are maximal at a controlled fructose concentration of 50 g/L. In continuous feeding experiments, the maximum mannitol yield was 85% (g/g) at a glucose/fructose feeding ratio of 1/20. A high glucose concentration in the production phase resulted in the formation of ethanol followed by a decrease in yield and productivity. NAD(P)H-dependent mannitol dehydrogenase was purified to homogeneity from C. magnoliae. In vitro, mannitol dehydrogenase was inhibited by increasing ethanol concentration. Mannitol product was also found to be inhibitory with a K(i) of 183 mM. Under optimum conditions, a final mannitol production of 213 g/L was obtained from 250 g fructose/L after 110 h.     

Features of bacterial cellulose synthesis in a mutant generated by disruption of the diguanylate cyclase 1 gene of <Emphasis Type="Italic">Acetobacter xylinum</Emphasis> BPR 2001

The diguanylate cyclase 1 (DGC1) (dgc1) gene in Acetobacter xylinum BPR 2001—a bacterial cellulose (BC) producer—was cloned and sequenced, and a DGC1 gene-disrupted mutant, strain DD, was constructed. The production and structural characteristics of the BC formed by DD were compared with those of the parental strain BPR 2001. BC production by DD was almost the same as that by BPR 2001 in static cultivation and in shake flask cultivation. However, in a jar fermentor DD produced about 36% more BC than the parental strain. DD produced suspended particle materials that cannot aggregate owing to their random structural characteristics in static cultivation; more uniformly dispersed BC pellicles and smaller BC pellets are produced on average in a jar fermentor, as reflected by the higher BC production by DD than by the parental strain in a jar fermentor. Micrographs of BC produced by DD revealed that the width of cellulose ribbons assemblies decreased as a result of differences in the ultrastructure and mechanism of formation of BC between the two strains. These results reveal that disruption of the dgc1 gene, which catalyzes synthesis of c-di-GMP (an effector of BC synthase), is not fatal for BC synthesis, although it affects BC structure.     

Rhamnolipid production in batch and fed-batch fermentation using<Emphasis Type="Italic">Pseudomonas aeruginosa</Emphasis> BYK-2 KCTC 18012P

The optimization of culture conditions for the bacteriumPseudomonas aeruginosa BYK-2 KCTC 18012P, was performed to increase its rhamnolipid production. The optimum level for carbon, nitrogen sources, temperature and pH, for rhamnolipid production in a flask, were identified as 25 g/L fish oil, 0.01% (w/v) urea, 25 and pH 7.0, respectively. Optimum conditions for batch culture, using a 7-L jar fermentor, were 200 rpm of agitation speed and a 2.0 L/min aeration rate. Under the optimum conditions, on fish oil for 216 h, the final cell and rhamnolipid concentrations were 5.3 g/L and 17.0 g/L respectively. Fed-batch fermentation, with different feeding conditions, was carried out in order to increase, cell growth and rhamnolipid production by thePseudomonas aeruginosa, BYK-2 KCTC 18012P. When 2.5 g of fish oil and 100 mL basal salts medium, containing 0.01% (w/v) urea, were fed intermittently during the fermentation, the final cell and rhamnolipid concentrations at 264 h, were 6.1 and 22.7 g/L respectively. The fed-batch culture resulted in a 1.2-fold increase in the dry cell mass and a 1.3-fold increase in rhamnolipid production, compared to the production of the batch culture. The rhamnolipid production-substrate conversion factor (0.75 g/g) was higher than that of the batch culture (0.68 g/g).     

Large-scale production of anthocyanin by Aralia cordata cell suspension cultures

The suspension culture of high anthocyanin-producing Aralia cordata cell lines, which grow and produce anthocyanin without light irradation, was scaled up from flasks to a 10-1 glass jar fermentor, a 95-1 stainless steel jar fermentor, and finally a 500-l pilot-scale jar fermentor. By the administration of CO₂, cell damage was completely prevented and the anthocyanin content was kept as high as 7.0–17.2% (w/w) of the dried cells. In one of the operations of the 500-l jar fermentor, cells were cultivated for 16 days. During this operation, cell mass was increased by more than 26 times (cell yield: 69.2 kg fresh wt.) and the amount of anthocyanin increased by more than 55 times (anthocyanin yield: 545 g, anthocyanin content: 17.2% of the dried cells). Correspondence to: Y. Kobayashi     

代谢工程改造大肠杆菌合成丁二酸及发酵罐放大工艺

【背景】Escherichia coli AFP111发酵生产丁二酸时大量副产乙酸,丁二酸得率低。【目的】代谢工程改造EscherichiacoliAFP111,提高丁二酸得率,降低副产物乙酸的生成,建立100 L规模的丁二酸发酵工艺。【方法】一步同源重组敲除乙酸合成途径关键酶基因,改造丁二酸合成途径关键酶启动子实现过表达;单因素优化5L发酵罐培养条件。【结果】敲除乙酸产生途径编码乙酸激酶和磷酸转乙酰酶的基因ackA-pta、苏氨酸脱羧酶和2-酮丁酸甲酸裂解酶的基因tdcDE获得SX02菌株,摇瓶发酵条件下其乙酸产量下降了53.42%,丁二酸得率提高9.85%。在SX02菌株基础上,经启动子改造过表达编码葡萄糖激酶的基因glk后获得菌株SX03,其Glk酶活性提高3.66倍,乙酸产量下降了31.62%,丁二酸得率提高8.28%。SX03菌株发酵生产丁二酸在5 L发酵罐进行放大,其乙酸产量为3.97 g/L,丁二酸得率为1.62 mol/mol葡萄糖,相比出发菌株的乙酸产量下降了75.76%,丁二酸得率提高19.12%。在5L发酵罐上对比研究了中和剂Na2CO3和NaOH混合液替换碱式MgCO3的发酵效果,并优化了发酵pH、搅拌转速和葡萄糖浓度,获得如下最适发酵条件:pH6.8,搅拌转速250r/min,葡萄糖100g/L,发酵结束时乙酸产量为2.24 g/L,丁二酸得率为1.66 mol/mol葡萄糖。中和剂替换优化后乙酸产量下降了20.65%,丁二酸得率提高2.47%。菌株SX03发酵工艺进一步在100 L发酵罐上实现放大,其乙酸产量为1.91 g/L,丁二酸得率为1.30 mol/mol葡萄糖。【结论】通过代谢工程改造的大肠杆菌,其副产物乙酸含量显著下降,丁二酸得率提高,并在5 L和100 L发酵罐上实现了工艺放大,展现出较大的工业化利用潜力。     

Optimization of culture conditions in CO2 fixation for succinic acid production using Actinobacillus succinogenes

The culture conditions in CO(2) fixation by Actinobacillus succinogenes for succinic acid production were investigated by a model of available CO(2) in a 3-l fermentor. The results from the model analysis showed that the available CO(2) for succinic acid production in the fermentation broth is the sum of HCO(3) (-), CO(3) (2-), and CO(2) influenced by external culture conditions such as medium components, CO(2) partial pressures, and temperature. The optimized conditions for CO(2) supply in a 3-l fermentor were determined as follows: CO(2) partial pressure and stirring speed were maintained at 0.1 MPa and 200 r min(-1), respectively, with a pH of 6.8 and a temperature of 37°C; 0.15 mol l(-1) NaHCO(3) was added. Under the optimized conditions, a CO(2) fixation rate of 0.57 g l(-1) h(-1) was obtained, and a succinic acid concentration of 51.6 g l(-1) with a yield of 75.8% was reached. These results suggest that optimized conditions of CO(2) supply are effective in high succinic acid production and thus have potential applications in succinic acid production and CO(2) fixation.     

Increase of xylitol production rate by controlling redox potential in Candida parapsilosis

The effect of redox potential on xylitol production by Candida parapsilosis was investigated. The redox potential was found to be useful for monitoring the dissolved oxygen (DO) level in culture media, especially when the DO level was low. An increase in the agitation speed in a 5 L fermentor resulted in an increased culture redox potential as well as enhanced cell growth. Production of xylitol was maximized at a redox potential of 100 mV. As the initial cell concentration increased from 8 g/L to 30 g/L, the volumetric productivity of xylitol increased from 1.38 g/L. h to 4.62 g/L. h. A two-stage xylitol production strategy was devised, with stage 1 involving rapid production of cells under well-aerated conditions, and stage 2 involving cultivation with reduced aeration such that the culture redox potential was 100 mV. Using this technique, a final xylitol concentration of 180 g/L was obtained from a culture medium totally containing 254.5 g/L xylose in a 3,000 L pilot scale fermentor after 77 h fermentation. The volumetric productivity of xylitol during the fermentation was 2.34 g/L. h.     

Effects of dissolved oxygen on the morphology of an arachidonic acid production by Mortierella alpina 1S-4

Arachidonic acid (AA) production by Mortierella alpina 1S-4 was investigated using a 50-L fermentor. In order to optimize the dissolved oxygen (DO) concentration and to investigate the effect of DO on morphology, cultivation was carried out under constant DO at various levels in the range of 3-50 ppm. To maintain a DO concentration above 7 ppm, two methods, i.e., the oxygen-enrichment (OE) method (experimental range, 25-90% oxygen gas supplied) and the pressurization (PR) method (experimental range, 180-380 kPa headspace pressure), were used. As a result, the optimum DO concentration range was found to be 10-15 ppm. In this optimum DO concentration range, the AA yield was enhanced about 1.6-fold compared to that obtained at 7 ppm DO, and there was no difference in the AA productivity between the OE and PR methods. When the DO concentration was maintained at 20-50 ppm using the OE method, the morphology changed from filaments to pellets, and the AA yield decreased drastically because of stress due to the limited mass transfer through the pellet wall. When the DO concentration was maintained at 15-20 ppm using the PR method, the morphology did not change, and the AA yield decreased gradually.     

Effect of ventilation on the production of acetaldehyde by Zymomonas mobilis

The production of acetaldehyde, a flavoring agent in food, by Zymomonas mobilis was carried out in batch culture. The volatilization rate constant (k_v) of acetaldehyde and the initial volumetric oxygen transfer coefficient (k_La⁰) in an Erlenmeyer flask with a cotton-plug (cotton-flask) and an aerated-flask with a forced-air system (aerated-flask) were measured. The culture environment in the aerated-flask was found to be very different from that in the cotton-flask. Cell growth in a cotton-flask was strongly inhibited, making practical acetaldehyde production in cotton-flask very difficult. On the other hand, acetaldehyde production in the aerated-flask increased while the fermentation time decreased with increases in the air flow rate. The k_v value of acetaldehyde in a jar fermentor was affected mainly by air flow rate. By considering both the oxygen transfer rate and the ventilation effect on the culture, it was possible to scale-up from the aerated-flask to a jar fermentor. In the jar fermentor, production of acetaldehyde and growth inhibition by acetaldehyde were affected mainly by the k_La⁰ and k_v, values, respectively. The overall production of acetaldehyde in the jar fermentor under the optimum k_La⁰ and k_v conditions was 6.64 g/l (Y_p/s: 0.27), which was about 1.5 times higher than the maximum concentration obtained in the aerated-flask.