混合碳源发酵生产头孢菌素C过程优化

本文对头孢菌素C（Cephalosporin C,CPC）发酵过程中碳源补料控制策略进行了优化研究,提出了一种基于DO—Stat的混合碳源流加策略,提高了发酵整体性能。在7L发酵罐上对使用该策略和传统补油策略的头孢菌素发酵性能进行比较,结果表明,采用补加混合碳源（葡萄糖＋豆油）策略时,CPC终浓度最高,达到36．99g／L,CPC得率也从使用传统单纯补油策略时的11．39％提高到22．19％,代谢副产物去乙酰氧头孢菌素C（DAOC）的积累量少,DAOC／CPC只有0．38％,达到生产要求。     

抗生素和干扰素

951655溶解氯浓度对头孢菌素一C生物合成的影响[英]/Zhou,W.…矿~nzyme.Microb.Techn01.-1992,14(10).一848~854[译自DBA,1992,11(23),92—129543 在含复合培养基(补加50g/l花生粉)的401搅拌式发酵罐中,在工业条件下批式进料培养Acre-mo≈lt‘m chrysogenum W53.2.53,产生头孢菌素-C(CPC)。研究了生产期间5～40％饱和的溶解氧浓度(pO:,DOC)的作用。将pOt由tO％降低到5％饱和浓度,~ICPC浓度由7.2g/1降至1.1g/l,青霉素N(AD)浓度由2.5zg/l增至7.65Ill。脱乙酰头孢菌素一C浓度也由3.13降至0.42g/1,但对DAOC、AC和ACV的浓度影响…     

真养产碱杆菌积聚-β-羟基丁酸发酵条件的研究

igenes eutrophus培养过程的研究表明,氮源的限制或缺乏可刺激细胞大量积累聚-β-羟基丁酸(PHB),但PHB合成期氮源的完全缺乏,会导致细胞的PHB合成速率迅速下降;氧的限制也可刺激A.eutrophus合成PHB,但胞内PHB的积累量远小于氮源控制下的情况。在细胞的不同生长期限制氮源的供应会明显影响PHB的发酵过程,当残留菌体浓度达到20g/L至30g/L时停止流加氨水,可以得到较好的发酵水平,细胞干重,PHB含量和PHB浓度可分别达到61.9g/L、80.5%和49.0g/L。     

利用三阶段葡萄糖添加策略减少乙酸合成并促进重组大肠杆菌生产L-苯丙氨酸

为了降低副产物乙酸的积累和提高L-苯丙氨酸的产量,分别优化了L-苯丙氨酸发酵的初始葡萄糖浓度和葡萄糖的指数流加策略.结果表明,20 g/L的初始葡萄糖浓度可以控制细胞的比生长速率低于临界值0.3 h-1,显著地降低了乙酸的积累,提高了L-苯丙氨酸的产量.采用预设比生长速率μ3* =0.4(h-1)进行葡萄糖的指数流加取得了实际最大比生长速率0.29 h-1,使细胞的比生长速率低于临界值,促进了L-苯丙氨酸的合成,最终获得L-苯丙氨酸的产量达48.45 g/L,比本实验室原有水平提高了37％.     

氧载体对小白链霉菌发酵生产ε-聚赖氨酸的影响

为了有效改善发酵体系中的溶氧水平,提高小白链霉菌Streptomyces albulus PD-1发酵生产ε-聚赖氨酸的能力,文中通过对氧载体的种类、最佳添加浓度以及添加时间进行筛选,最终确定在0 h添加0.5%(V/V)的正十二烷促进ε-聚赖氨酸生产效果最佳。在5 L发酵罐0 h添加0.5%的正十二烷进行批次补料发酵,ε-聚赖氨酸的产量和菌体干重分别可以达到(30.8±0.46)g/L和(33.8±0.29)g/L,较之对照组分别提高了31.6%和20.7%。ε-聚赖氨酸的产量和菌体干重的提高归因于0.5%正十二烷的添加促进发酵液中溶氧水平从23.8%提高到32%,同时发酵液中的一种主要副产物(聚二氨基丙酸)的含量下降31%。实验结果表明,正十二烷的添加可以提高S.albulus PD-1发酵液中的溶氧水平,抑制副产物的生成,促进ε-聚赖氨酸的合成。     

发酵生产7-ACA基因工程菌的构建

头孢菌素类抗牛素是临床用途最广的抗感染药物,其工业生产的重要中间体7－氨基头孢烷酸（7－ACA）采用顶头孢霉发酵产物头孢菌素C为前体,通过化学合成或两步酶法狭得。介绍了在了解头孢菌素C生物合成的前提下,在建赢了顶头孢霉的遗传改造丛础上,运用合成生物学的知识,在头孢菌素C产生菌顶头孢霉中分别构建了三个头孢菌素C酰化酶的表达框架,通过发酵产物的分析并优选表达框架后,再采用传统发酵工艺的优化获得了一株可以直接发酵7-ACA的高产顶头孢霉工程菌。     

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WSH2601（Rhizobium radiobacter WSH2601）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Q₁₀的影响,结果表明, 葡萄糖和蔗糖适合于生产辅酶Q₁₀的最佳浓度分别为30 g/L和40 g/L;辅酶Q₁₀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Q₁₀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Q₁₀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Q₁₀的产量,最大产量达到52.4 mg/L;最大生物量（DCW）和胞内辅酶Q₁₀含量（C/B值）分别达到26.4 g/L和2.38 mg/g-DCW,比不流加的分批发酵分别提高53%和33%,比只流加蔗糖分别提高24%和26%。     

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 %。     

克雷伯氏肺炎杆菌LDH526产1,3-丙二醇的甘油自动流加策略

1,3-丙二醇是一种重要的化工原料,主要作为平台化合物用于合成聚酯,如聚对苯二甲酸丙二醇酯。经基因工程改造的克雷伯氏肺炎杆菌LDH526能以甘油作为唯一碳源合成1,3-丙二醇,最终发酵浓度超过90 g/L。甘油浓度是影响1,3-丙二醇合成的关键因素。为了实现对甘油浓度的精确控制,设计并优化了基于发酵动力学的甘油自动流加策略。通过将底物流加速率与易观察变量p H和发酵时间偶联,实现了发酵过程中甘油流加的自启动和甘油浓度的动态控制。发酵72 h,1,3-丙二醇的浓度可稳定超过95 g/L。自动控制甘油流加的发酵过程具有可重复性、连续性以及人工工作量少的特点,有望从实验室规模扩大到生产规模。     

菌丝形态分化与头孢菌素C合成的关系*

利用显微图像分析法对顶头孢霉菌的菌丝形态进行了定量研究,并统计分析了头孢菌素C发酵过程中的菌丝形态的变化规律,具体对菌丝长度、菌丝宽度和菌丝生长单位进行了定量分析,分析了菌丝形态分化与头孢菌素C合成的关系。研究表明头孢菌素C的合成是在细长菌丝分化成膨大菌丝片段后才启动的,头孢菌素C可能主要是在膨大菌丝分化成节孢子的过程中被合成。     

Performance improvement of cephalosporin C fermentation by Acremonium chrysogenum with DO-Stat based strategy of co-feeding soybean oil and glucose

Cephalosporin C (CPC) fermentation by Acremonium chrysogenum featured with two major problems: (1) high raw materials cost (low CPC yield from soybean oil) and (2) low oxygen transfer rate between gaseous/aqueous phases leading to low CPC productivity and quality instability of CPC fermentation product due to the accumulation of deacetoxycephalosporin C (DAOC). To solve the problems, in this study, we proposed a novel DO-Stat based co-substrates feeding strategy by simultaneously supplementing soybean oil and glucose, and testified the effectiveness of the strategy in a 7 L bioreactor. The CPC fermentation performance were significantly improved when co-feeding soybean oil and glucose at a weight ratio of 1:0.7, as compared with those when feeding pure soybean oil: (1) final CPC concentration and yield reached higher levels of 37 g/L and 23.5%, the increments were 46% and 82%, respectively; (2) oxygen transfer rate was largely improved, oil consumption rate and CPC productivity were enhanced by 31% and 136%, respectively; and (3) DO could be controlled at adequately high levels so that DAOC accumulation could be minimized and the quality of CPC fermentation product be ensured. The proposed strategy showed application potential in improving the economics of industrial CPC productions.     

Use of soybean oil and ammonium sulfate additions to optimize secondary metabolite production

A valine-overproducing mutant (MA7040, Streptomyces hygroscopicus) was found to produce 1.5 to 2.0 g/L of the immunoregulant, L-683,590, at the 0.6 m3 fermentation scale in a simple batch process using soybean oil and ammonium sulfate-based GYG5 medium. Levels of both lower (L-683,795) and higher (HH1 and HH2) undesirable homolog levels were controlled adequately. This batch process was utilized to produce broth economically at the 19 m3 fermentation scale. Material of acceptable purity was obtained without the multiple pure crystallizations previously required for an earlier culture, MA6678, requiring valine supplementation for impurity control. Investigations at the 0.6 m3 fermentation scale were conducted, varying agitation, pH, initial soybean oil/ammonium sulfate charges, and initial aeration rate to further improve growth and productivity. Mid-cycle ammonia levels and lipase activity appeared to have an important role. Using mid-cycle soybean oil additions, a titer of 2.3 g/L of L-683,590 was obtained, while titers reached 2.7 g/L using mid-cycle soybean oil and ammonium sulfate additions. Both higher and lower homolog levels remained acceptable during this fed-batch process. Optimal timing of mid-cycle oil and ammonium sulfate additions was considered a critical factor to further titer improvements.     

在线推定和控制葡萄糖浓度改善谷氨酸发酵性能

谷氨酸发酵过程一般需要定时、人工分批式地添加葡萄糖。该流加操作方式会引起发酵罐内葡萄糖浓度的剧烈波动, 不利于高效、稳定的谷氨酸生产。谷氨酸发酵具有显著的非增殖耦联特征, 产酸期葡萄糖耗量与氨水耗量存在非常明显的关联性。通过在线计量氨水耗量推定糖耗以及葡萄糖浓度, 可比较准确地将谷氨酸发酵产酸期的糖浓度控制在预先设定的水平。当糖浓度控制在5 g/L~10 g/L的低水平时, 最终谷氨酸浓度可以达到80 g/L的较高水平, 高糖浓度下的渗透压效应有望得到缓解, 有利于发酵生产的稳定。     

Morphology and kinetics studies on cephalosporin C production by Cephalosporium acremonium M25 in a 30-l bioreactor using a mixture of inocula

AIMS: In this study, the relationship between morphology and cephalosporin C (CPC) production in a 30-l bioreactor culture of Cephalosporium acremonium M25 using a 3:7 seed mixture was investigated. In addition, the kinetic model was established and applied. METHODS AND RESULTS: CPC production was performed in a 30-l bioreactor using a 3:7 seed mixture. It was recognized that a 3:7 seed mixture was able to reduce lag phase and enhance CPC production. The maximum CPC production and cell mass were 1.96 and 81.5 g l-1 respectively. Through a morphology study by observation using image analysis, it was concluded that changes of morphological features predicted the progressive production of CPC and that a morphology study could be useful in monitoring the CPC fermentation by C. acremonium M25. In the kinetics study, a kinetic model of CPC fermentation was developed and applied. The proposed model could adequately describe the fermentation of C. acremonium M25 in a 30-l bioreactor. CONCLUSIONS: CPC productivity was improved by using a 3:7 seed mixture in a 30-1 bioreactor. The changes in morphological features showed a very similar tendency with CPC production. A kinetic model of CPC fermentation was successfully established. SIGNIFICANCE AND IMPACT OF THE STUDY: The results of the present study suggest that the use of a 3:7 seed mixture inocula has considerable possibilities for improving CPC productivity if applied to industrial scale fermentations. Through morphology and kinetics study, the kinetic model to describe the morphological differentiation and CPC production by C. acremonium M25 was established.     

Influence of medium composition on the cephalosporin C production with a highly productive strain Cephalosporium acremonium.

Cephalosporin production by a highly productive Cephalosporium acremonium strain was carried out and optimized by fed-batch operation in a 40 l stirred tank reactor using a complex medium containing 30-120 g l-1 peanut flour. The concentrations of cephalosporin C (CPC) and its precursors: penicillin N (PEN N), deacetoxy cephalosporin C (DAOC), and deacetyl cephalosporin C (DAC) were monitored with an on-line HPLC. The concentrations of amino acids valine (VAL), cysteine (CYS), alpha-amino adipic acid (alpha-AAA), the dipeptide alpha-amino-adipyl-cysteine (AC), and the tripeptide alpha-amino-adipyl-cysteinyl-valine (ACV), were determined off-line by HPLC. The RNA content and dry weight of the sediment as well as the oxygen transfer rate (OTR) and the CO2 production rate (CPR) were used to calculate the cell mass concentration (X). The influences of peanut flour (PF) and the on-line monitored and controlled medium components: glucose (GLU), phosphate, methionine (MET) as well as the dissolved oxygen (DOC) on the cell growth, the product formation, and the pathway of cephalosporin C biosynthesis were investigated and evaluated. When the glucose fed-batch cycle was optimized and oxygen transfer limitation was avoided (DOC greater than 20% of the saturation value), high process performance (103.5 g l-1 X, 11.84 g l-1 CPC, a maximum CPC productivity of 118 mg l-1 h-1, and the whole concentration of the beta-lactam antibiotics CPC, DAC, DAOC, PEN N 17.34 g l-1) was achieved by using 100 g l-1 PF in the medium with the optimum concentration of phosphate (260-270 mg l-1) and a low glucose concentration (less than 0.5 g l-1). The cultivations with different medium concentrations demonstrated that the product formation was directly proportional to the cell mass concentration. On the average, the cell mass-based yield coefficient of CPC: YCPC/X amounted to 0.115 g CPC per g cell mass.     

Expression of cefF significantly decreased deacetoxycephalosporin C formation during cephalosporin C production in Acremonium chrysogenum

Deacetoxycephalosporin C (DAOC) is not only the precursor but also one of the by-products during cephalosporin C (CPC) biosynthesis. One enzyme (DAOC/DAC synthase) is responsible for the two-step conversion of penicillin N into deacetylcephalosporin C (DAC) in Acremonium chrysogenum, while two enzymes (DAOC synthase and DAOC hydroxylase) were involved in this reaction in Streptomyces clavuligerus and Amycolatopsis lactamdurans (Nocardia lactamdurans). In this study, the DAOC hydroxylase gene cefF was cloned from Streptomyces clavuligerus and introduced into Acremonium chrysogenum through Agrobacterium tumefaciens-mediated transformation. When cefF was expressed under the promoter of pcbC, the ratio of DAOC/CPC in the fermentation broth significantly decreased. These results suggested that introduction of cefF could function quite well in Acremonium chrysogenum and successfully reduce the content of DAOC in the CPC fermentation broth. This work offered a practical way to improve the CPC purification and reduce its production cost.     

Influence of dissolved oxygen concentration on the biosynthesis of cephalosporin C.

Cephalosporin C was produced by a highly productive strain of Cephalosporium acremonium under industrial production conditions by fed-batch cultivation in a 40-l stirred-tank reactor using a complex medium containing 50 g l-1 peanut flour. The influence of dissolved oxygen concentration (pO2, DOC), which was maintained at different constant levels between 5 and 40% of its saturation value, during the production phase by means of a parameter-adaptive pO2-controller, on the cephalosporin C biosynthesis, was investigated. The concentrations of cephalosporin C (CPC) and its precursors penicillin N (PEN N), deacetoxycephalosporin C (DAOC), and deacetylcephalosporin C (DAC) were monitored by on-line HPLC. The concentrations of amino acids, valine (VAL), cysteine (CYS), alpha-amino-adipic acid (alpha-AAA), the dipeptide alpha-amino-adipyl-cysteine (AC), and the tripeptide alpha-amino-adipyl-cysteinyl-valine (ACV) were determined by off-line HPLC. By reducing the pO2 in the production phase from 40 to 5% of its saturation value, the CPC concentration diminished from 7.2 to 1.1 g l-1 and the PEN N concentration increased from 2.57 to 7.65 g l-1. The DAC concentration also dropped from 3.13 to 0.42 g l-1; however, the DAOC concentration was less influenced. The concentrations of AC and ACV were also less affected. The small DOC did not lead to an accumulation of the intermediate AC and ACV during the production phase. With increasing DOC in the range of 5-20%, the maximal specific production rate, the cell mass concentration-based and the substrate-based yield coefficients for CPC increased almost linearly, and fell back for PEN N.(ABSTRACT TRUNCATED AT 250 WORDS)     

休哈塔假丝酵母乙醇发酵性能的研究

木糖的高效发酵是制约纤维素燃料乙醇生产的技术瓶颈之一,高性能发酵菌种的开发是本领域研究的重点。以木糖发酵的典型菌株休哈塔假丝酵母为材料,研究氮源配比、葡萄糖和木糖初始浓度、葡萄糖添加及典型抑制物等因素对其木糖利用和乙醇发酵性能的影响规律。结果表明,硫酸铵更适宜于木糖和葡萄糖发酵产乙醇。在摇瓶振荡发酵条件下,该酵母可发酵164.0 g/L葡萄糖生成61.9 g/L乙醇,糖利用率和乙醇得率分别为99.8%和74.0%;受酵母细胞膜上转运体系的限制,对木糖的最高发酵浓度为120.0 g/L,可生成45.7 g/L乙醇,糖利用率和乙醇得率分别达到94.8%和87.0%。休哈塔假丝酵母发酵木糖的主要产物为乙醇,仅生成微量的木糖醇;添加葡萄糖可促进木糖的利用;休哈塔假丝酵母在葡萄糖发酵时的乙酸和甲酸的耐受浓度分别为8.32和2.55 g/L,木糖发酵时的乙酸和甲酸的耐受浓度分别为6.28和1.15 g/L。     

Effects of the addition of different nitrogen sources in the tequila fermentation process at high sugar concentration

AIMS: To study the effect of the addition of different nitrogen sources at high sugar concentration in the tequila fermentation process. METHODS AND RESULTS: Fermentations were performed at high sugar concentration (170 g l(-1)) using Agave tequilana Weber blue variety with and without added nitrogen from different sources (ammonium sulfate; glutamic acid; a mixture of ammonium sulfate and amino acids) during the exponential phase of growth. All the additions increased the fermentation rate and alcohol efficiency. The level of synthesis of volatile compounds depended on the source added. The concentration of amyl alcohols and isobutanol were decreased while propanol and acetaldehyde concentration increased. CONCLUSIONS: The most efficient nitrogen sources for fermentation rate were ammonium sulfate and the mixture of ammonium sulfate and amino acids. The level of volatile compounds produced depended upon types of nitrogen. The synthesis of some volatile compounds increased while others decreased with nitrogen addition. SIGNIFICANCE AND IMPACT OF THE STUDY: The addition of nitrogen could be a strategy for improving the fermentation rate and efficiency in the tequila fermentation process at high sugar Agave tequilana concentration. Furthermore, the sensory quality of the final product may change because the synthesis of the volatile compounds is modified.