搅拌转速和pH对ε-聚赖氨酸发酵的影响

采用5L自控式发酵罐研究了ε-聚赖氨酸分批发酵过程中搅拌转速和pH对发酵指标以及菌体细胞形态的影响。提高搅拌速率对菌生长和ε-赖氨酸的合成有显著的促进作用;但当搅拌转速达到400r／min以上时,由于剪切力过大导致细胞死亡,ε-聚赖氨酸产量下降。当pU维持5以上,有利于菌体生长;pH4．0左右可促进￡一聚赖氨酸的合成。搅拌转速350r／min和控制pH4．0时可获得最大的￡一聚赖氨酸产量2．95g/L,菌体量9．33g／L;此时产物E．聚赖氨酸对葡萄糖的得率和对细胞干重的比生成速率分别为0．062g／g和0．006g／g．h。通过对比不同发酵条件下ε丝体的形态变化,发现当菌丝球比较均匀、形态无较大差别、具有致密程度相当的核心时,有利于￡一聚赖氨酸形成。     

调控pH提高分批发酵赤霉素GA3产量

为高效率发酵生产GA₃,对藤仓赤霉菌发酵过程pH进行优化调控研究。采用5L全自动发酵罐,在pH 3.0-5.0条件下,对藤仓赤霉菌菌丝生长及GA₃产量的影响进行了考察,实验数据表明：在pH 4.0条件下,菌比生长速率可获最大值,为0.395/h;而pH 3.0条件下,GA₃比生成速率最大,达到4.43mg/(g?h)。基于不同pH条件下,对菌比生长速率、得率、GA₃比生成速率的影响,提出GA₃分批发酵过程中的pH调控策略,即：0-20h,pH自然;20-50h,pH 4.0;50-80h,pH 3.0-3.5;80h后控制pH为3.5-4.0。在此控制模式下,经过196h发酵GA₃的终产量达到2 224mg/L,GA₃产率44.5mg/g,GA₃生产强度0.242mg/(L?h),分别比不控制pH条件下发酵的数值增长了7.75%、7.74%、8.04%,表明该pH控制策略能增进GA₃发酵生产效率。     

枯草芽孢杆菌(Bacillus subtilis)发酵生产乙偶姻的pH调控策略

【目的】为了提高Bacillus subtilis CCTCC M 208157发酵生产乙偶姻的效率。【方法】在7 L发酵罐水平上考察不同pH条件对菌株生长及乙偶姻合成的影响。【结果】pH对菌株合成乙偶姻有显著影响,pH 4.5有利于细胞合成乙偶姻,但是延迟期较长;pH 5.5时菌株生长较快,但乙偶姻的产量偏低。因此提出了两阶段pH控制策略:发酵前期(0 16 h),控制pH 5.5;发酵中后期(16 72 h),控制pH 4.5。【结论】通过此策略,菌株合成乙偶姻的能力得到进一步提高,乙偶姻的产量、产率和生产强度分别为32.7 g/L、0.41 g/g和0.91 g/(L.h),分别比初始发酵条件下提高了41%、42%和69%。     

静息细胞转化生产3-羟基丙酸的条件优化

本文研究了静息细胞生物转化生产3-羟基丙酸的反应体系。考察了以甘油为底物,利用静息细胞转化生产3一羟基丙酸的相关因素,确定了最佳的转化条件：细胞浓度20g／L,甘油浓度20g／L,辅酶VB12浓度10mg／L,NAD＋浓度0．15mmol／L,温度35℃,反应体系为0．05mol／LpH7．0Tris—HCl缓冲液。在上述条件下反应6h后,3-羟基丙酸的产量达到为3．17g／L,底物转化率为28．33％。由上述结果可知,采用静息细胞转化法为3-HP的生物合成提供了一种可能的方法。     

两阶段搅拌转速控制策略发酵生产聚唾液酸

目的:优化聚唾液酸发酵过程的搅拌转速.方法:比较不同搅拌转速对大肠杆菌Escherichia coli K235分批发酵生产聚唾液酸过程的影响.结果:根据发酵前、后期菌体细胞比生长速率和聚唾液酸比合成速率达到最大值所需搅拌转速的不同,提出了两阶段搅拌转速控制策略:发酵前期(0～15h)控制搅拌转速500r/min,发酵中后期控制搅拌转速700r/min.结论:两阶段搅拌转速控制策略使聚唾液酸产量达到3 966mg/L,比恒定搅拌转速500r/min和700r/min分别提高了31.8%和49.3%.将两阶段搅拌转速控制策略与分批补料发酵技术结合,聚唾液酸产量提高到5 108mg/L,山梨醇的转化率达到0.12g/g.     

赤霉素发酵溶氧优化调控研究

为了解溶氧对赤霉素发酵过程影响以及相应工艺优化,采用不同溶氧条件下藤仓赤霉菌Gibberella fujikuroi分批发酵生产赤霉素的过程进行菌丝浓度、残糖浓度和GA3产物浓度检测,并微分运算得出比生长速率与比产物合成速率随发酵时间变化,分析了溶氧对比生长速率与比产物合成速率以及得率的影响,进而提出Gibberella fujikuroi发酵高产的溶氧控制策略:在发酵初始阶段(0–50h)控制溶氧30%左右,以维持较高的菌体生长速率;发酵中后期(50–184h),溶氧控制在15%,以获取菌丝持续较高的GA3合成速率能力。采用这一优化溶氧控制策略,发酵过程中最大菌丝浓度19.24g/L、最终赤霉素浓度2 180mg/L和平均比产物合成速率0.616mg/(g·h),比未优化前发酵分别提高了8.33%、13.25%和4.58%,表明所采取的分阶段溶氧控制策略对促进GA3生产有效。     

pH两阶段控制策略发酵生产重组角质酶

为提高基因工程菌Bacillus subtilis WSHB06-07发酵生产角质酶的产量和生产强度,考察了pH（5.5~8.0）对菌体生长和产酶的影响。基于不同pH发酵过程中菌体比生长速率及比产物合成速率的变化,确定了pH两阶段控制策略,即0~4 h时控制pH 7.5,4 h后将pH调至6.5。通过采用这一优化策略,角质酶酶活有了较大的提高,达170 U/mL,生产强度为16.9 kU/(L·h),比恒定pH 7.5控制模式下分别提高了122.6%和123.2%。     

环境条件及摇瓶补糖策略对谷胱甘肽发酵的影响

研究了酵母摇瓶发酵中pH、装液量、初糖浓度、碳氮磷比和补糖方式对谷胱甘肽(GSH)发酵的影响。结果表明,GSH发酵适宜的初始pH和装液量分别为6 0和500ml锥形瓶内装液量60m1。初糖浓度对GSH发酵有较大的影响,超过12g／l,的初糖浓度将减少胞内GSH含量。应用计算得出的一种以控制比生长速率为目的的摇瓶补糖策略,在总糖浓度为26．2g／L下发酵12h,最终细胞浓度和胞内GSH含量分别达到8.78g／L和13．6mg／g,发酵液内GSH总量达到119．4mg／L,细胞对糖产率达到0.335g／g。     

pH值对D-核糖发酵的影响及补料发酵的研究

研究了不同 pH值对D 核糖产量的影响。发酵初期pH自然下降时有利于菌体生长 ,菌体生长对数期较长 ,菌体质量浓度最高可达 15 .3g/L ;发酵中后期 pH值控制在 7.0时有利于D 核糖的持续合成 ,同时对D -核糖的流加补料发酵进行了初步研究 ,最终使菌体质量浓度最高达到 2 0 .1g/L ,D 核糖产量达到了 6 2 .5g/L。     

环境条件对丙酮酸分批发酵的影响

考察了搅拌转速、pH和温度对丙酮酸分批发酵的影响。高转速（500r／min）下,丙酮酸产率较高（71％）,但葡萄糖消耗速度较慢（1．23g／（L·h））;低转速（300r／min）下,细胞消耗葡萄糖的速度加快（1．95g/（L·h））,而丙酮酸产率（0．48％）却明显下降。将搅拌转速恒定在400r／min可在一定程度上获得较高的丙酮酸产率（0．62％）和葡萄糖消耗速度（1．66g／（L·h））。CaCO3调节pH时,较多碳流从丙酮酸节点转向α-酮戊二酸节点和细胞生长,最终丙酮酸产量比NaOH调节pH时的发酵结果低38．7％;NH3·H2O调节pH时最终细胞浓度和丙酮酸产量仅为NaOH调节时的77．8％和90．9％。pH5．5时最利于丙酮酸的合成。较高的发酵温度加速T.glabrata积累丙酮酸,但同时会导致α-酮戊二酸的提前积累;而较低的温度下甘油和α-酮戊二酸积累较少,丙酮酸发酵的最适温度为28～30℃。     

分阶段pH调控提高2-酮基-L-古龙酸生产

为了提高酮古龙酸菌Ketogulonicigenium vulgare和巨大芽胞杆菌Bacillus megaterium生产2-酮基-L-古龙酸(2-KLG)的生产效率,分析了pH对K.vulgare和B.megaterium生长和产酸的影响,发现K.vulgare和B.megaterium的最适生长pH值分别为6.0和8.0,但是K.vulgare的糖酸转化活力在pH7.0时达到最大值,因此提出了三阶段pH控制策略(第一阶段:0～8h,pH8.0;第二阶段:8～20h,pH6.0;第三阶段:20h至发酵结束,pH7.0)以促进K.vulgare生长和2-KLG生产。结果表明,三阶段pH控制策略的实施进一步提高了2-KLG的产量(77.3g/L)、生产强度(1.38g/(L·h))和L-山梨糖消耗速率(1.42g/(L·h)),分别比恒定pH7.0时提高了9.7%、33.2%和25.7%。     

Influence of pH and impeller tip speed on the cultivation of<Emphasis Type="Italic">Bifidobacterium pseudocatenulatum</Emphasis> G4 in a milk-based medium

Biomass production ofBifidobacterium pseudocatenulatum G4 in a milk-based medium was carried out in a 2- and 10-L stirred tank fermenters. The effects of impeller tip speed (0.28, 0.56, and 0.83 m/s) and pH control (6.0, 6.5, and 7.0) on the biomass production were investigated. The growth performance in the 2-L fermenter was significantly improved when the impeller tip speed was held constant at 0.56 m/s and the pH was controlled at 6.5. These conditions yielded a maximum biomass of 1.687×10⁹ cfu/mL, a maximum specific growth rate of 0.504 h⁻¹, a biomass productivity of 9.240×10⁷ cfu/mL·h, and a biomass yield of 9.791×10¹⁰ cfu/g lactose. The consumption of milk lactose resulted in the accumulation of 7.353 g/L acetic acid and 6.515 g/L lactic acid, with an acetic:lactic ratio of 1.129. Scale-up of the fermentation process to a 10-L fermenter based on a constant impeller tip speed of 0.56 m/s yielded reproducible results with respect to biomass production and cell viability.     

Development of a two-step process for production of 3-hydroxypropionic acid from glycerol using <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> and <Emphasis Type="Italic">Gluconobacter oxydans</Emphasis>

In this work, a two-step process was developed for the production of 3-hydroxypropionic acid from glycerol. In the first step, glycerol was converted to 1,3-propanediol by Klebsiella pneumonia. In the second step, the 1,3-propanediol was converted into 3-hydroxypropionic acid by Gluconobacter oxydans. In a 7.0 L bioreactor, the whole process took 54 h, consumed 480 g glycerol and produced 242 g 3-hydroxypropionic acid. The conversion rate of glycerol to 3-hydroxypropionic acid was 50.4 % (g g^?1). The final concentration of 3-hydroxypropionic acid arrived 60.5 g L^?1. The process was effective for 3-HP production from glycerol and it might provide a new approach to the biosynthesis of 3-HP from a cheap starting material. Moreover, in this paper, it was first reported that the by-product of 3-hydroxypropionic acid production from 1,3-propandeiol was acrylic acid.     

Efficient docosahexaenoic acid production by Schizochytrium sp. via a two-phase pH control strategy using ammonia and citric acid as pH regulators

The cell growth and docosahexaenoic acid (DHA) synthesis of Schizochytrium sp. are closely related to the culture pH. A two-phase pH control strategy based on nitrogen consumption was developed in which pH 7.0 was used for biomass accumulation and pH 5.0 for DHA synthesis. Using this strategy, the cell dry weight and DHA content reached 98.07 and 25.85 g/L, respectively. Furthermore, ammonia and citric acid were used as pH regulators. Application of citric acid further resulted in 7.88 and 4.87% improvements of total lipids and the ratio of DHA to total fatty acids, respectively. Ammonia, as a suitable nitrogen source, promoted non-lipid biomass accumulation. Using this method, a maximum DHA yield of 32.75 g/L was obtained with non-lipid biomass (58.01 g/L) and the ratio of DHA to total fatty acids (52.36%). This study provides an easy strategy for large-scale industrial production of DHA via high-cell-density fermentation of Schizochytrium sp.     

Factors influencing biohydrogenation and conjugated linoleic acid production by mixed rumen fungi

The objective of this study was to evaluate the effect of soluble carbohydrates (glucose, cellobiose), pH (6.0, 6.5, 7.0), and rumen microbial growth factors (VFA, vitamins) on biohydrogenation of linoleic acid (LA) by mixed rumen fungi. Addition of glucose or cellobiose to culture media slowed the rate of biohydrogenation;only 35-40% of LA was converted to conjugated linoleic acid (CLA) or vaccenic acid (VA) within 24 h of incubation, whereas in the control treatment, 100% of LA was converted within 24 h. Addition of VFA or vitamins did not affect biohydrogenation activity or CLA production. Culturing rumen fungi at pH 6.0 slowed biohydrogenation compared with pH 6.5 or 7.0. CLA production was reduced by pH 6.0 compared with control (pH 6.5), but was higher with pH 7.0. Biohydrogenation of LA to VA was complete within 72 h at pH 6.0, 24 h at pH 6.5, and 48 h at pH 7.0. It is concluded that optimum conditions for biohydrogenation of LA and for CLA production by rumen fungi were provided without addition of soluble carbohydrates, VFA or vitamins to the culture medium; optimum pH was 6.5 for biohydrogenation and 7.0 for CLA production.     

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）。     

Effects of pH and aeration on gamma-poly(glutamic acid) formation by Bacillus licheniformis in controlled batch fermentor cultures

Bacillus licheniformis ATCC 9945A was grown on Medium E in batch fermentations in which the pH was maintained at 5.5., 6.5, 7.4, and 8.25. The effects of pH on cell growth, carbon source utilization, and gamma-polyglutamic acid (gamma-PGA) production, molecular weight, and polymer stereochemistry were determined. The gamma-PGA yield was highest (15 g/L, 96 h growth time) at pH 6.5. The increase in gamma-PGA formation at pH 6.5 corresponded with a relatively high specific production rate at high gamma-PGA concentration (0.09 h(-1), approximately 15 g/L gamma-PGA). In contrast, the specific gamma-PGA production rates at fermentor pH values of 5.5 and 7.4 decreased significantly for gamma-PGA fermentor yields > approximately 5 g/L. Interestingly, alteration of the medium pH had little to no significant effects on the product quality as measured by stereochemical composition and molecular weight. While glutamate and glycerol utilization were similar as a function of pH, citrate consumption increased at pH 6.5, indicating that the formation of gamma-PGA from citrate at pH 6.5 was of increased importance. The effect of aeration was evaluated by increasing the agitation speed (250 to 800 rpm) and aeration rate (0.5 to 2.0 L/min) at pH 6.5, the pH of maximal gamma-PGA production. Increased aeration resulted in doubling of the cell dry weights (2 to 4 g/L), increasing gamma-PGA yields (6.3 to 23 g/L by 48 h) and increasing in the maximum gamma-PGA-specific production rate (0.09 to 0.11 h(-1)). Other effects of increased agitation included a rapid depletion of glutamate and citrate (by 50 h) and a decrease in product molecular weight. Despite the increase in agitation and aeration, oxygen limitation of the culture was not avoided, because the partial pressure decreased to <1.0% by 29 h. (c) 1996 John Wiley & Sons, Inc.     

pH对槐角愈伤组织黄酮类化合物产量的影响

培养基酸碱度是影响植物生长和次生代谢的重要因素之一。将生长稳定的国槐槐角愈伤组织在不同pH值的B5悬浮培养基中培养,比较其生长状况、生物量及苯丙氨酸转氨酶活性和黄酮类化合物的产量。结果表明:pH为6.6时,国槐细胞生长状况好,且不同pH下的苯丙氨酸转氨酶活性差异显著;培养基呈弱酸性(即6.6±0.05)时,细胞黄酮类化合物含量较高。综合生长天数和产量,最佳的收获时期为继代后的第25～30天。