氨水流加用于粪产碱杆菌热凝胶发酵

热凝胶是粪产碱杆菌(Alcaligenes faecalis)在氮源限制条件下生成的水不溶性胞外多糖,分泌到胞外后就附着在菌体外壁,因此在细胞生长期提高生物量对促进热凝胶合成有重要意义。热凝胶分批发酵时, 起始NH4Cl浓度提高到3.6 g/L时能促进菌体生长和热凝胶合成,但是过量NH4Cl会抑制热凝胶合成,且生物量提高不是很明显。为了进一步提高菌体浓度, 在菌体生长期, 氨水取代NaOH溶液进行流加控制pH为7.0, 随后又用2 mol/L NaOH控制pH 5.6。实验表明, 氨水流加使菌体浓度大大提高,流加24 h使菌体浓度达到18.8 g/L。但是菌体浓度过高也会抑制热凝胶的合成,在氨水流加14 h时,菌体浓度在11.9 g/L左右, 热凝胶产量最高（72 g/L）。     

氨水流加用于粪产碱杆菌热凝胶发酵

热凝胶是粪产碱杆菌(Alcaligenes faecalis)在氮源限制条件下生成的水不溶性胞外多糖,分泌到胞外后就附着在菌体外壁,因此在细胞生长期提高生物量对促进热凝胶合成有重要意义。热凝胶分批发酵时, 起始NH4Cl浓度提高到3.6 g/L时能促进菌体生长和热凝胶合成,但是过量NH4Cl会抑制热凝胶合成,且生物量提高不是很明显。为了进一步提高菌体浓度, 在菌体生长期, 氨水取代NaOH溶液进行流加控制pH为7.0, 随后又用2 mol/L NaOH控制pH 5.6。实验表明, 氨水流加使菌体浓度大大提高,流加24 h使菌体浓度达到18.8 g/L。但是菌体浓度过高也会抑制热凝胶的合成,在氨水流加14 h时,菌体浓度在11.9 g/L左右, 热凝胶产量最高（72 g/L）。     

氮源NH4Cl浓度对粪产碱杆菌发酵生产热凝胶的影响

研究了利用粪产碱杆菌(Alcaligenes faecalis)发酵生产热凝胶的发酵条件,氮源是菌体生长的限制性底物,单纯地提高初始底物(氮源)浓度并不一定能促进细菌的生长和产物的合成.在分批发酵过程中,底物消耗导致培养环境pH的改变也是影响细菌进一步生长和产物合成的重要因素.通过增加培养基中初始氯化铵的浓度并同时控制发酵过程的pH条件,得到了较高的菌体浓度,热凝胶的合成水平也得到了显提高.当培养基中NH4Cl浓度提高到3.6g/L时,菌体浓度达到7.2g/L,热凝胶合成的产量可达30.5g/L,比原来NH4Cl浓度为1.1g/L时提高了51.7%.提高菌体浓度意味着需要提高溶氧水平来满足细菌的生长和代谢.初始氮源NH4Cl浓度的增加虽然能使菌体浓度得到提高,但发酵过程对溶氧的需求也相应增加,需要提高搅拌转速和通风以增加供氧水平.但高搅拌速率产生的高剪切力对热凝胶的凝胶性能将产生破坏作用,因此在发酵过程中需要综合考虑细菌培养密度对合成热凝胶产量和质量的影响.     

Improved production of curdlan with concentrated cells ofAgrobacterium sp.

The addition of a limited concentration of yeast extract to a minimal salt medium (MSM) enhanced cell growth and increased the production of curdlan whereas nitrogenlimitation was found to be essential for the higher production of curdlan byAgrobacterium sp. ATCC 31749. As the amount of the inoculum increased, the cell growth as well as the production of curdlan also increased in the MSM without a nitrogen source. The cell growth and production of curdlan increased as the initial pH of the medium decreased as low as 5.0. The conversion rate and concentration of curdlan from 2% (w/v) glucose in the MSM with concentrated cells under nitrogen deletion was 67% and 13.4 g/L, respectively. The highest conversion rate of curdlan under the conditions optimized in this study was 71% when the glucose concentration was 1% (w/v).     

Optimization and production of curdlan gum using Bacillus cereus PR3 isolated from rhizosphere of leguminous plant

Curdlan gum is a neutral water-insoluble bacterial exopolysaccharide composed primarily of linear β-(1,3) glycosidic linkages. Recently, there has been increasing interest in the applications of curdlan and its derivatives. Curdlan is found to inhibit tumors and its sulfated derivative possess anti-HIV activity. Curdlan is biodegradable, non-toxic towards human, environment and edible which makes it suitable as drug-delivery vehicles for sustained drug release. The increasing demand for the growing applications of curdlan requires an efficient high yield fermentation production process so as to satisfy the industrial needs. In this perspective, the present work is aimed to screen and isolate an efficient curdlan gum producing bacteria from rhizosphere of ground nut plant using aniline-blue agar. High yielding isolate was selected based on curdlan yield and identified as Bacillus cereus using gas-chromatography fatty acid methyl ester analysis. B. cereus PR3 curdlan gum was characterized using FT-IR spectroscopy, SEM, XRD and TGA. Fermentation time for curdlan production using B. cereus PR3 was optimized. Media constituents like carbon, nitrogen and mineral sources were screened using Plackett–Burman design. Subsequent statistical analysis revealed that Starch, NH₄NO₃, K₂HPO₄, Na₂SO₄, KH₂SO₄ and CaCl₂ were significant media constituents and these concentrations were optimized for enhancement of curdlan production up to 20.88?g/l.     

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.     

A two stage continuous process for the production of thermogelable curdlan-type exopolysaccharide

Summary A laboratory-scale, two-stage continuous process for the production of curdlan-type exopolysaccharide has been operated in steady-state for 500hr. Two continuous flow, constant volume fermenters are connected in series. A stable, curdlan-producing strain of Alcaligenes faecalis var myxogenes ATCC 31749 is grown aerobically in a nitrogen-limited chemostat operating near D_max at 0.24 hr^–1. The effluent is introduced directly into a second larger constant volume fermenter which is being simultaneously fed a glucose solution at a fixed rate. Under sub-optimal conditions associated with curdlan production, the observed Qp was 0.05 g curdlan/g cell/hr. At a biomass level of 4 g/L in the second stage, curdlan was present at 10 g DW/L and the volumetric productivity was 0.2 g/g cell/hr. The substrate (glucose) conversion efficiency was 42%. The process is described in patents applied for on behalf of George Weston Ltd. (Toronto, Canada).     

pH控制对热凝胶发酵的影响

热凝胶 (Ｃｕｒｄｌａｎ)是一种直链结构的 β 1,3 葡聚糖 ,由Ａｌｃａｌｉｇｅｎｅｓｆａｅｃａｌｉｓｖａｒ.ｍｙｘｏｇｅｎｅｓ发酵生产而来 ,是一种新型的微生物胞外多糖[1 ] ,其分子量在 5 0万左右。热凝胶在中性条件下不溶于水 ,但能溶于碱溶液中。加热含有热凝胶的水浊液可形成两种类型的凝胶 ,一种是弹性较低的类似琼脂的可逆胶 ;另外一种是凝胶强度大、弹性好的热不可逆胶。由于热凝胶具有独特的热成胶性能 ,在食品工业 ,特别是高温制作的食品领域具有广阔的应用前景。热凝胶的胶体可以包容和控制药物的扩散 ,所以可以用来作为药物…     

Optimization of a liquid medium for beauvericin production in <Emphasis Type="Italic">Fusarium redolens</Emphasis> Dzf2 mycelial culture

Beauvericin (BEA) is a proven and potent antibiotic compound useful for bio-control and a potential antifungal and anticancer agent for human. This study was to evaluate and optimize the nutrient medium for BEA production in mycelial liquid culture of a high BEA-producing fungus Fusarium redolens Dzf2 isolated from a medicinal plant. Among various organic and inorganic carbon and nitrogen sources, glucose and peptone were found the most favorable for the F. redolens Dzf2 mycelial growth and BEA production. Through a Plackett-Burman screening test on a basal medium, glucose, peptone, and medium pH were identified as the significant factors for mycelial growth and BEA production. These factors were optimized through central composite design of experiments and response surface methodology, as 49.0 g/L glucose, 13.0 g/L peptone and pH 6.6, yielding 198 mg/L BEA (versus 156 mg/L in the basal medium). The BEA yield was further increased to 234 mg/L by feeding 10 g/L glucose to the culture during exponential phase. The results show that F. redolens Dzf2 mycelial fermentation is a feasible and promising process for production of BEA.     

Optimal pH control of batch processes for production of curdlan by Agrobacterium species

We sought an optimal pH profile to maximize curdlan production in a batch fermentation of Agrobacterium species. The optimal pH profile was calculated using a gradient iteration algorithm based on the minimum principle of Pontryagin. The model equations describing cell growth and curdlan production were developed as functions of pH, sucrose concentration, and ammonium concentration, since the specific rates of cell growth and curdlan production were highly influenced by those parameters. The pH profile provided the strategy to shift the culture pH from the optimal growth condition (pH 7.0) to the optimal production one (pH 5.5) at the time of ammonium exhaustion. By applying the optimal pH profile in the batch process, we obtained significant improvement in curdlan production (64 g L⁻¹) compared to that of constant pH operation (36 g L⁻¹). Received 24 November 1998/ Accepted in revised form 17 June 1999     

Optimal production of curdlan by Agrobacterium sp. with feedback inferential control of optimal pH profile

The pH control was important for curdlan production with Agrobacterium sp. ATCC31750. Specific cell growth rate was the highest at pH 7 and the specific curdlan production rate was at pH 5.5. The pH profiles maximizing curdlan production was changed from pH 7 optimal for cell growth to pH 5.5 optimal for curdlan production after ammonium consumption. The feedback inferential control methods, with easily measurable variables such as NaOH addition for pH control and dissolved oxygen (DO), were also applied. The pH was successfully controlled to follow optimal profiles and the maximal production of curdlan (60 g l^–1 in 120 h) was achieved with feedback optimal control.     

A robust fed-batch feeding strategy independent of the carbon source for optimal polyhydroxybutyrate production

A three-stage control strategy independent of the organic substrate was developed for automated substrate feeding in a two-phase fed-batch culture of Cupriavidus necator DSM 545 for the production of the biopolymer polyhydroxybutyrate (PHB). The optimal feeding strategy was determined using glucose as the substrate. A combined substrate feeding strategy consisting of exponential feeding and a novel method based on alkali-addition monitoring resulted in a maximal cell concentration in the biomass growth phase. In the PHB accumulation phase, a constant substrate feeding strategy based on the estimated amount of biomass produced in the first phase and a specific PHB accumulation rate was implemented to induce PHB under limiting nitrogen at different biomass concentrations. Maximal cell and PHB concentrations of 164 and 125 g/L were obtained when nitrogen feeding was stopped at 56 g/L of residual biomass; the glucose concentration was maintained within its optimal range. The developed feeding strategy was validated using waste glycerol as the sole carbon source for PHB production, and the three-stage control strategy resulted in a PHB concentration of 65.6 g/L and PHB content of 62.7% while keeping the glycerol concentration constant. It can thus be concluded that the developed feeding strategy is sensitive, robust, inexpensive, and applicable to fed-batch culture for PHB production independent of the carbon source.     

粗甘油优化污泥脱水液培养小球藻过程的研究

污泥脱水液为污泥压缩过程产生的污水,因其含有N、P等营养物,可用于微藻的培养。但污泥脱水液碳氮比低,可利用碳源有限,影响微藻生长。本研究考察外加不同浓度(1 g/L,2 g/L,4 g/L,6 g/L)生物柴油副产物-粗甘油对污泥脱水液培养小球藻过程的影响。结果表明:1 g/L、2 g/L粗甘油浓度能促进小球藻生长,藻生物量为1.29 g/L、1.45 g/L;2 g/L粗甘油浓度下氨氮、总氮去除率达99.32%和97.52%。粗甘油被分解后易使培养体系pH降至7以下,使总磷去除率比对照组略低。外加1 g/L、2 g/L粗甘油组的COD去除量分别为553.00 mg/L和405.00 mg/L。藻细胞元素和傅里叶红外光谱分析表明补加粗甘油后藻细胞中C元素和H元素相对含量均明显增加,C元素含量约为对照组的1.5倍;2 g/L粗甘油组的蛋白质与脂类物质含量均高于对照组。MPBR半连续培养小球藻过程中,HRT为5 d时藻生物量维持在1.99~2.21 g/L,大约为批次生物量的1.50倍;氨氮、总氮、总磷、COD的去除率分别在96.26%~99.20%、92.44%~94.04%、53.63%~58.58%、59.44%~65.57%。     

Utilization of rice bran as nutrient source for fermentative lactic acid production

To reduce nutrient cost for lactic acid production, rice bran, one of agricultural wastes, was chosen as a nutrient source in this study. Although rice bran is rich in protein and vitamins, the use of rice bran without any treatment was inefficient in lactic acid production. Rice bran was treated by acid-hydrolysis before it was put in experiment, when it was hydrolyzed at initial pH 1, 30 g/L rice bran could provide a productivity to that degree of about 8 g/L YE, showing such a desirable result that the use of rice bran as nutrient source would be a solution for reducing nutrient cost. However, the addition of hydrolyzed rice bran prolonged lag phase of fermentation, especially, in the fermentation with rice bran hydrolyzed at initial pH 0.5, a prolonged lag phase of about 40 h was observed. According to the quantitative determination of thiamine, pyridoxine, organic nitrogen and carbon, the prolongation of lag phase might be the result from the destruction of B vitamins and excessive hydrolysis of protein. To shorten the lag phase, combining hydrolyzed rice bran with yeast extract (YE) of small amount was considered to be a solution. When 3g/L YE was combined with 30 g/L rice bran hydrolyzed at initial pH 1, obtained was a productivity 1.6 times higher than that of the control fermentation with 15 g/L YE.     

Production of curdlan using sucrose or sugar cane molasses by two-step fed-batch cultivation of Agrobacterium species

Maltose and sucrose were efficient carbon sources for the production of curdlan by a strain of Agrobacterium sp. A two-step, fed-batch operation was designed in which biomass was first produced, followed by curdlan production which was stimulated by nitrogen limitation. There exists an optimal timing for nitrogen limitation for curdlan production in the two-step, fed-batch operation. Maximum curdlan production (60 g L⁻¹) was obtained from sucrose with a productivity of 0.2 g L⁻¹ h⁻¹ when nitrogen was limited at a cell concentration of 16.0 g L⁻¹. It was also noted that the curdlan yield from sucrose was as high as 0.45 g curdlan g⁻¹ sucrose, and the highest specific production rate was 1.0 g curdlan g⁻¹ cells h⁻¹ right after nitrogen limitation. Of particular importance was the use of molasses as a cheap carbon source to produce curdlan in the two-step, fed-batch cultivation. As high as 42 g L⁻¹ of curdlan with a yield of 0.35 g curdlan g⁻¹ total sugar was obtained after 120 h of fed-batch cultivation. Received 20 August 1996/ Accepted in revised form 26 November 1996     

长孢被孢霉利用淀粉质原料发酵产微生物油脂

通过研究长孢被孢霉(Mortierella elongate)的发酵过程,并采用摇瓶分批补料发酵模式考察了起始补料时间及补料基质对长孢被孢霉合成微生物油脂的影响。结果发现该菌株合成油脂主要在发酵48~96 h进行,且N源对菌株的生长有促进作用,采用限氮补料发酵可大幅度提高微生物油脂的产量。最适培养条件:可溶性淀粉20 g/L,玉米浆3 g/L,补料起始时间为发酵48 h,单次补加可溶性淀粉4 g。在此条件下,油脂产量较不补料时增加了521.74 mg,增长率为237.1%。     

Optimization of uracil addition for curdlan (β-1→3-glucan) production by Agrobacterium sp.

Uracil, acting as a precursor of UDP-glucose, served as an activator on the production of curdlan with Agrobacterium sp. (ATCC 31750). The time of adding uracil was important to improve curdlan production. When uracil was added after ammonium depletion (at 26 h), it was used as a nitrogen source for cell growth. Although the cell concentration increased, the curdlan production was decreased. If uracil was added at 46 h, then uracil was degraded slowly but still activated curdlan production. With the addition of both sucrose (200 g) and uracil (1.5 g), the curdlan production was increased up to 93 g l^–1 after 160 h fermentation.     

Continuous operation of foamed emulsion bioreactors treating toluene vapors

Continuous operation of a new bioreactor for air pollution control called the foamed emulsion bioreactor (FEBR) has been investigated. The effect of several liquid feeding strategies was explored. The FEBR exhibited high and steady toluene removal performance (removal efficiency of 89%-94%, elimination capacity of 214-226 g/m3h at toluene inlet concentration of 1 g/m3) for up to 360 h, when 20% of the culture was replaced every 24 h by a nutrient solution containing 4 g/L of potassium nitrate as a nitrogen source. This feeding mode supported a high cell activity measured as INT reduction potential and active cell growth without being subject to nitrogen limitation. In comparison, operating the FEBR with the liquid in a closed loop (i.e., batch) resulted in a significant decrease of both the removal efficiency of toluene and INT reduction activity. Operation with feeding active cells resulted in stable and effective treatment, but would require a significant effort for mass culture preparation. Therefore, the continuous process with periodically feeding nutrients was found to be the most practical and effective operating mode. It also allows for stable operation, as was shown during removal of low concentration of toluene or after pollutant starvation. Throughout the study, INT reduction measurements provided insight into the process. INT reduction activity data proved that under normal operating conditions, the FEBR performance was limited by both the kinetics and by mass transfer. Overall, the results illustrate that engineered gas-phase bioreactors can potentially be more effective than conventional biofilters and biotrickling filters for the treatment of air pollutants such as toluene.     

Study of mycelial growth and bioactive polysaccharide production in batch and fed-batch culture of Grifola frondosa

The fermentation of Grifola frondosa was investigated in the shake flasks and a 5-L jar fermenter in batch and fed-batch modes. In the shake-flask experiments, the preferable mycelial growth and exopolysaccharide (EPS) production was observed at relatively low pH; maltose and glucose were preferred carbon sources for high mycelial production. The EPS was doubled after 13 d of cultivation when glucose was increased from 2% to 4%. Yeast extract (YE) (0.4%) in combination with corn steep powder (CSP) (0.6%) and YE (0.8%) in combination with CSP (1.2%) were preferred nitrogen sources for high mycelial production and EPS production, respectively. All plant oils tested significantly stimulate cell growth of G. frondosa but they failed to enhance EPS production. The EPS products usually consisted of two fractions of different molecular sizes varied by the plant oils used. The fed-batch fermentation by glucose feeding was performed when the glucose concentration in the medium was lower than 0.5% (5g/L), which greatly enhanced the accumulation of mycelial biomass and EPS; the mycelial biomass and EPS were 3.97g/L and 1.04g/L before glucose feeding, which reached 8.23g/L and 3.88g/L at 13 d of cultivation. In contrast, the mycelial biomass and EPS in the batch fermentation were 6.7g/L and 3.3g/L at 13 d of cultivation.     

Effective extracellular production of Bacillus stearothermophilus esterase by pH-stat modal fed-batch culture of recombinant Bacillus brevis

An automated two-component substrate feeding strategy with a pH-stat modal fed-batch culture using a high pH limit was developed to effectively porduce esterase from a hyperprotein exreting Bacillus brevis HPD31 harboring a plasmid pHSC131 which carries a Bacillus stearothermo philus esterase gene. First, the effect of single- and multi-substrate feedings on the growth and activity of the excreted esterase was investigated. Then a two-component (polypepton + glucose) feeding using different feed rates was studied. Highest activity of the excreted esterase (34 U/mL) was obtained when the concentrations of poly-pepton and glucose in the nutrient feed solution were 250 and 41.60 g/L respectively. The absence and excessive amount of glucose in the nutrient feed solution was ineffective for the exracellular esterase formation because without glucose the increase in cell concentration was minimum while excessive amount of glucose favored cell growth at the expense of the esterase production. It is believed that the mechanism of enzyme excretion is growth dependent and that a higher cell growth of the host is in effect unfavorable for the enzyme production. The feed rate, automatically controlled by the direct signal of the pH change, at 0.30 mL/pulse was found optimum for the esterase production while lower (0.15 mL/pulse) and higher (0.67 mL/pulse) feed rates did not produce good results. The activity of the excreted esterase was increased more than eight times from 4 U/mL obtained in the conventional batch culture to 34 U/mL obtained in this study. The esterase productivity was likewise increased more than threefold. (c) 1992 John Wiley & Sons, Inc.